Here - Wetsus

Transcription

Here - Wetsus

May 26-28, Leeuwarden
IAP
Interfaces in Water and
2014 Environmental Science
I
Wetsus is co-funded by
• the Dutch Ministry of Economic Affairs (IOP-TTI, Peaks in the Delta)
• the Dutch Ministry of Infrastructure and the Environment
• the European Union (European Fund for Regional Development and Seventh
Framework Programme)
• Northern Netherlands Provinces (REP-SNN)
• the City of Leeuwarden, the Province of Fryslân and University Campus Fryslân
II
Leeuwarden, City Center
III
Welcome
IAP conferences seek to provide a forum for researchers working in the interdisciplinary field of Environmental Science. Colloids and lnterfaces in natural and engineered media are at the heart of the conference. This includes topics of societal concerns like environmental protection, remediation of polluted sites,
water treatment, optimization of mineral resources and the impact of nanotechnology residues on the
environment.
IAP has a broad, but fundamentally scientific scope, which has broadened over the years. The IAP 2014
specifically has shown to attract a large community in the field of capacitive desalination. In line with the
wide spectrum of disciplines (physics, biology, physical chemistry, mineralogy) relevant for environmental
science, IAP2014 is intended to cover research from work at the nano-, meso- and macroscopic scales,
from transient processes to equilibrium.
The international IAP advisory council and the local IAP2014 organization committee would like to thank
our sponsors Gemeente Leeuwarden, Provinsje Fryslân, Wetsus, Water Campus Leeuwarden, Voltea, IACIS
and ISE for enabling this conference.
The international IAP advisory board and the local IAP2014 organization committees wish that this conference will be an opportunity for all participants to share fruitful discussions, in Leeuwarden.
Conference chairs
Prof. Dr. David Waite (University of New South Wales, Australia),
Dr. Bert Hamelers (Wetsus, The Netherlands)
Mayor Ferd. J.M. Crone of the City of Leeuwarden, capital of the province of Fryslân:
Welcome to Leeuwarden, the European Capital of Culture 2018!
Leeuwarden is a dynamic city which is situated in a green and water-rich environment.
The city has a watery heart and a heart for water.
The abundance of water is a defining feature of the city’s image and atmosphere. The recovery of water, energy, food and resources has a high priority. In addition, water is an important factor in the research and development of water
technology and sustainability. The expansion of the Water Campus Leeuwarden
is a good example of this.
I wish you an interesting congress and enjoy your visit to Leeuwarden, the
Capital of Water Technology.
1
General
The 8th International Conference Interfaces Against Pollution (IAP2014), held in Leeuwarden, the Netherlands from May 25 to 28, is part of a proud series of conferences initiated in Wageningen (The Netherlands, 1997) and followed in Miskolc (Hungary, 2002), Julich (Germany, 2004), Granada (Spain, 2006),
Kyoto (Japan, 2008) , Beijing (China, 2010) and most recently in Nancy.
General
About the organization
Conference chairs
Dr. Bert Hamelers
Conference chair
Wetsus, Netherlands
Prof. Dr. David Waite
Chair IAP council
UNSW, Australia
Prof. Dr. Luuk Koopal
Founder of IAP
WUR, Netherlands
Dr. Maarten Biesheuvel
co-chair
Prof. Dr. Volker Presser
co-chair
Dr. Jan Post
conference director
Oane Galama
Jouke Dykstra
Hester Henstra
Linda van der Ploeg
Vytautas Abromaitis
Joeri de Valença
Local organizing committee
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Questions?
General
In case you have questions about general issues, the local organizing committee can help you.
During the conference you can contact them the following ways:
- ask the committee members in person;
- go to the information desk of De Harmonie;
- send an e-mail to [email protected] (we will answer your mail during the conference);
- call +31(0)6 46 24 70 80
International scientific committee
Yasu Adachi (Japan) Maarten Biesheuvel (Wetsus, Netherlands, co-chair) Rob Comans (Wageningen, Netherlands) Jerome Duval (France) Bert Hamelers (Wetsus, Netherlands, chair) Hong He (China) Guido Mul (Twente, Netherlands) Volker Presser (INM, Germany, co-chair) Louis de Smet (Delft, Netherlands) David Waite (Australia)
International advisory council
Yasuhisa Adachi (Japan) Marcelo Avena (Argentina) Philippe Behra (France) Maarten Biesheuvel (Netherlands) Michal Borkovec (Switzerland) Scott Bradford (USA) Andrzej Dabrowski (Poland) Angel Delgado (Spain) Jerome Duval (France) Menachim Elimelech (USA) Fernando Gonzalez-Caballero (Spain) Ellen Graber (Israel) John Gregory (UK) Hong He (China) Stephan Hug (Germany) Erwin Klump (Germany) Luuk Koopal (Netherlands) Nataliya Mishchuk (Ukraine) Jiuhui Qu (China) Etelka Tombacz (Hungary) Raewyn Town (Denmark) David Waite (Australia) Kevin Wilkinson (Canada)
Frontpage courtesy J. de Valença “Dynamics of micro-vortices in ion-exchange membranes”
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General
General information
Conference location
The conference location is De Harmonie, Leeuwarden. De Harmonie is Leeuwarden’s city theatre, located
in the old city centre. Leeuwarden is a beautiful small old and historical city with royal connections and an
extensive canal network.
The address of De Harmonie is: Stadsschouwburg De Harmonie Ruiterskwartier 4 8911 BP Leeuwarden The Netherlands
Internet service
There is free wireless internet available in City Theatre de Harmonie.
The following login details are required:
Login:
IAP-congress
Password:
IAP2014
Oral presentations
There are two ways to turn in your oral presentation (.pdf, .pptx, .ppt):
- to e-mail your presentation at least 24h in advance to [email protected].
- to hand in your presentation on a flash drive (usb stick, thumb drive) in the morning before start of the
program at the central registration desk near the entrance in De Harmonie, not in the conference rooms!
Poster presentations
Please bring your poster to the exhibition floor of De Harmonie (ground floor) from 08.30 - 09.30 on Monday, where we will assist you to put up your poster.
Poster prize award
Besides oral presentations, there is a special poster presentation session. This will be held on Monday 26th
of May from 17.00 – 18.00 PM on the ground floor of our conference center: ‘De Harmonie’. During this
session researchers are given the opportunity to explain to, and discuss about their scientific research topic with the visiting audience. Members of the Poster Prize Committee will assess the quality of the poster
and the interaction with interested attendees. The poster prize ceremony will be held during the dinner
on Tuesday in De Grote of Jacobijnerkerk.
We wish all participants good luck and fruitful interactions with the attendees.
Questions?
In case you have questions about general issues, the local organizing committee can help you.
During the conference you can contact them the following ways:
- ask the committee members in person;
- go to the information desk of De Harmonie;
- send an e-mail to [email protected] (we will answer your mail during the conference);
- call +31(0)6 46 24 70 80
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Social program
Reception, Monday, 18.00, De Harmonie
On Monday after the poster session, there is an Italian style buffet reception at De Harmonie, the City
Theatre of Leeuwarden, the conference location of IAP2014.
Conference dinner, Tuesday, 18.30, Grote of Jacobijnerkerk
On Tuesday, there is the Conference Dinner in De Grote of Jacobijnerkerk in Leeuwarden. The location is
pointed out on the map, which you can find on the backcover of this conference book. During the conference dinner former president and founder of IAP, Prof. Dr. Luuk Koopal, will share his view on the “past,
present, and future of IAP.”
Luuk Koopal worked at the Laboratory of Physical Chemistry and Colloid
Science of Wageningen University, NL. Since 2007 he is Guest Professor
at Wageningen University and at the College of Resources and Environment, Huazhong Agricultural University in Wuhan, P.R. China. He has
served IUPAC as Chairman of the Colloid and Surface Chemistry Commission and as member of the Bio-Physical Chemistry Division and is Past
President of the International Advisory Board of the IAP conferences. His
research interests are: interaction of ions, surfactants and nano-particles
with mineral surfaces and humic substances, and their effects on colloid
stability, wetting and flotation.
Visit at Wetsus or Fries museum, Wednesday, 15.00
On Wednesday, at 15.00 PM, there are two optional excursions:
- to the Fries museum, where you can see 170,000 objects of Frisian art, culture and history;
- to Wetsus, where we will show you the laboratory and research facilities.
On Monday, when you register for the conference, you will receive a registration form for these optional
excursions. If you like to attend, you can hand in this form before leaving De Harmonie on Monday. Alternatively, you can send an e-mail with your choice to [email protected] on Monday.
Former conferences
The 8th International Conference on Interfaces against Pollution (IAP) to be held in Leeuwarden (2014),
lies within the framework of a series of conferences held previously in:
•
Nancy (France, 2012)
•
Beijing (China, 2010)
•
Kyoto (Japan, 2008)
•
Granada (Spain, 2006)
•
Jülich (Germany, 2004)
•
Miskolc (Hungary, 2002)
•
Wageningen (The Netherlands, 1997)
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General
Welcoming reception, Sunday, 17.30, The city hall of Leeuwarden
The conference starts with a welcoming reception in the City Hall of Leeuwarden, Hofplein 38 in Leeuwarden, on Sunday May 25.
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Paul Tratnyek - Oregon Health and Science University, USA - Reactivity of Iron Nanoparticles: Spectroscopy, Electrochemistry, Kinetics, and Environmental Implications (page 14) (Rabobank zaal, chair: Bert Hamelers)
Soraya
Heuss-Aßbichler
Mineralogical
investigations of precipitates obtained by treatment
of Cu-rich waste water by Ferrite process (page 27)
He Zhao - Cross-coupling oxidation of bisphenol A
during electro-enzymatic oxidative process (page
28)
Benedicte Prelot - Interactions of organic dyes with
layered double hydroxides (page 29)
Manuel Nuño - Study photocatalytic reactions for
pollution remediation by electron ionisation mass
spectrometry (page 30)
Coffee
Catalysis and electrochemistry:
carbon materials
Chair: David Wesolowski
Mickaël Gineys - Reversible trapping of water
contaminants on nanoporous carbon electrodes
(page 22)
Laurent Duclaux - Adsorption kinetics and isotherms
of micropollutants onto activated carbon fabric and
felt (page 23)
Xu Zhao - Electrochemical reduction of haloacetic
acids in a three-dimensional electrochemical reactor
with Pd-GAC particles as fixed filler and Pd-modified
carbon paper as cathode (page 25)
Yael Mishael - Developing Efficient Polycation-Clay
Sorbents for the Removal of Pharmaceuticals and
Dissolved Organic Matter (page 26)
9.30-9.40
9.40-10.20
10.20-11.00
11.00 -12.20
Lunch
Hans Lyklema - Wageningen University, The Netherlands - Models of colloids and models for interpretation. A bit of history. (page 15)
(Rabobank zaal, chair: Maarten Biesheuvel)
12.20-13.00
13.00-13.40
Xiaowei Sun (k) - Applications of electrosorption
systems for waste water recovery (page 31)
Slawomir Porada (k) - Electrodes in motion for
water desalination and energy harvesting (page
32)
Kelsey Hatzell (k) - CDI based on flowable electrodes
(page 33)
Eran Avraham (k) - Water desalination by CDI –
advantages and limitations (page 34)
Chair: Bert van der Wal
Processes in CDI
Welcoming ceremony (Bert Hamelers, Cees Buisman, David Waite) (Rabobank zaal)
Adsorption in environmental processes :
analytical methods & organic chemistry
Chair: Ellen Graber
Registration desk open and coffee
8.30
CDI Symposium – Bentacera zaal
IAP 1 – Rabobank zaal
Monday
IAP 2 – Nivo Noord zaal
General
He Jie - Heterogeneous Fenton oxidation of catechol
and 4-chlorocatechol catalyzed by nano-magnetite:
role of the interface reaction (page 46)
Julien Muller - Synthesis and complexation properties
of new polyvinyl alcohol (PVA)-based chelating
polymers (page 47)
Gaelle Gassin - Non linear optical tools to study ions
remediation processes (page 48)
Jie Ye - Preparation of γ-AlOOH loaded-zeolites and
characteristics for phosphate adsorption (page 49)
Nora Sutton - Geochemical and microbiological
characteristics during in situ chemical oxidation and
in situ bioremediation at a diesel contaminated site
(page 43)
Loes Fasotte - Removal of MTBE from groundwater
by adsorption and catalyzed ozonation (page 44)
Elena Mejia Likosova - An Innovative 2-Stage Process
for the Recovery of Phosphorus and Recycling of
Ferric from Ferric Sludges Generated in Water and
Wastewater Treatment (page 45)
Poster session + drinks
Reception
17.00-18.00
18.00-19.30
Chair: Huub Rijnaarts
Adsorption in environmental processes:
analytical methods & organic chemistry
Chair: Yi-Fan Han
Catalysis and electrochemistry
15.30-16.50
Jihun Kim - Removal efficiency of high concentration
waste water using Capacitive Deionization Process
(page 50)
Alexandra Rommerskirchen - Batch mode and
continuous membrane capacitive deionization using
flowing carbon electrodes (page 51)
Patrick Curran - Hyper Salinity Desalination using
Atlantis RDI Capacitive Deionization Technology
(page 52)
Cleis Santos Santos - Capacitive Deionization
for Waste Water Re-use: Energy Efficiency
Considerations (page 53)
Chair: Jieshan Qui
Applications of CDI
Jieshan Qiu (k) - Carbon Nanofiber and Graphene
Composites made by Electrospinning for CDI (page
39)
Volker Presser - Effect of pore size and its dispersity
of porous carbon on capacitive deionization (page
40)
Chengzhi Hu - Preparation of a MnO2/Carbon
Composite Electrode for Electrosorptive Removal of
Heavy Metal from Water (page 41)
Karthik Laxman - Zinc oxide nanorods coated
carbon electrodes for improved energy efficient CDI
of brackish water (page 42)
Yi-Fan Han (k) - Free Radicals Generating from
Catalytic Decomposition of H2O2: New Strategies and
Applications (page 35)
Rob Lammertink - Fast Degradation In Immobilized
Photocatalytic Microreactors (page 37)
HansPeter Zöllig - Fast inhibition of direct ammonia
oxidation on thermally decomposed iridium oxide
films through a change in local pH (page 38)
Coffee
New materials in CDI
Chair: Maarten Biesheuvel
Catalysis and electrochemistry
Chair: Paul Tratnyek
15.10-15.30
13.50-15.10
General
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8
Transport and mass transfer at interfaces
Chair: Luewton L. Agostinho
Norazanita Shamsuddin - Effects of MF membranes
deformation and permeability on filtration of clay suspension and its solution chemistry (page 72)
Stylianou Stylianos - Modified Hydrophobic Ceramic Membranes: Use For Ozone Transfer To Water
(page 73)
Barbara Liszka - A pneumatic micro-fluidic device
for in-situ detection of mineral scaling at a membrane surface (page 74)
Amy Tsai - Momentum and mass transport over a
superhydrophobic bubble mattress: the influence of
interface geometry (page 75)
Coffee
Adsorption to engineered surfaces
Chair: Rob Lammertink
Helene Fallou - Dynamic adsorption of
pharmaceutical residues at trace concentrations
onto activated carbon cloths (page 68)
Alberto Tiraferri - Adsorption of chitosan from
aqueous solutions onto silica (page 69)
Shazia Ilyas - Sacrificial polymer layers for easy
membrane cleaning (page 70)
Yasuhisa Adachi - Colloidal flocculation of PSL
particle induced by an adsorption of polyelectrolyte
studied in relatively concentrated suspension (page
71)
11.40 -13.00
Luewton L. Agostinho (k) - Characterization of droplets
produced by electrospray emulsification (page 60)
Norbert Kuipers - Simultaneous production of high
quality water and electrical power from aqueous
feedstocks and waste heat by high pressure membrane distillation (page 61)
Krzysztof Trzaskus - Investigating the fouling stages
during membrane filtration of silica nanoparticle solutions (page 62)
Maike Gröschke - Transport of Sewage-borne Ammonium in a Floodplain Aquifer: Column Experiments with Aquifer Materials from the Yamuna
Floodplain in Delhi (India) (page 63)
Ellen Graber - Role of Surfaces in the Biochar Effect
(page 56)
John Gregory - Phosphate adsorption on hydrous
ferric oxide and its effect on the re-growth of broken
flocs (page 57)
Dung Viet Pham - Effect of phosphate sorption on
Ferralsol dispersion: Evaluation with stability ratio
and repulsive potential energy (page 58)
Behnam Akhavan - Plasma Polymer Coated Particles: A New Class of Adsorbents for Water Purification (page 59)
11.10-11.40
Transport and mass transfer at interfaces
Chair: Amy Tsai
Adsorption to engineered surfaces
Chair: Alberto Tiraferri
Angel Delgado - Temperature effects on energy
production by salinity exchange (page 76)
Lorenza Misuri - Functionalized activated carbon for
“capacitive mixing” energy production (page 77)
Sangho Chung - Ultrathin metal oxide coated
mesoporous carbon material for enhanced capacitive
deionization (page 78)
Jianyun Liu - Mesoporous carbon nanofiber
fabrication and its capacitive desalination application
(page 79)
Park Namsoo - CDI carbon electrode coated with ion
selective layer (page 80)
Capmix / New materials
Chair: Slawomir Porada
Frieder Mugele - Ion adsorption at mineral-electrolyte interfaces probed by high resolution Atomic
Force Microscopy (page 64)
Thomas Sweijen - Pore-scale study of processes and
transport in porous media; an overview (page 65)
Joeri de Valenca - The Dynamics of Micro-vortices
During Overlimiting Electrodialysis (page 66)
Sven Schlumpberger - Water Purification and Brine
Concentration by Shock Electrodialysis (page 67)
Desalination
Chair: Bert Hamelers
Michael Sander – ETH Zürich, Switzerland – Should I stay or should I go now: assessing electron transfer properties of organic and mineral phases using analytical
electrochemistry (page 16) (Rabobank zaal, chair: David Waite)
9.00-9.40
9.50-11.10
Coffee
8.30
Tuesday
General
(Bio-)polymer/water interaction and charge
effects
Chair: Luuk Koopal
15.00-16.20
18.30
Chia-Hung Hou - Study of Electrosorption Performance of Nanostructured Carbon Electrodes in CDI
(page 96)
Doo-Hwan Jung - Pore-structure of Activated Carbon
Fibers on CDI (page 97)
James Landon - Capacitive Deionization with
PZC-Modified Carbon Xerogel: Half-Cell and System
Analysis for Long-Term Operation (page 98)
Luuk Koopal - Protein humic acid interaction (page
90)
Elise Rotureau - A biophysicochemical approach for
assessing the dynamics of metal uptake by microorganisms (page 91)
Mikhail Borisover - Sorption of organic molecules
on environmental sorbents: driving water molecules
in or out? (page 92)
Dinner in De Grote of Jacobijnerkerk (location indicated on the map, which you can find on the back cover of this book)
Yassine Bentahar - Comparison of Arsenic Adsorption on clays from Morocco (page 93)
Juan Antelo - Attenuation of metal cations by iron
oxide minerals from acid mine drainage (page 94)
MA Weifang - Adsorption and aerobic biodegradation of three selected endocrine disrupting chemicals in artificial groundwater recharge with treated
reclaimed municipal wastewater (page 95)
Chair: Jouke Dykstra
(Bio-)polymer/water interaction and charge Case studies, transport and conversion
effects
Chair: Oane Galama
Chair: Michael Sander
16.50-17.50
Characterization of CDI
Coffee
Jeyong Yoon (k) - The importance of carbon electrode
material affecting the maximum deionization
performance in CDI process (page 85)
Li-Ching Chung - Insight in TiO2/AC electrodes
prepared by a microwave-assisted ionothermal
synthesis method for CDI (page 86)
Heena Mutha - Vertically-Aligned Carbon Nanotube
Electrodes for CDI (page 87)
Florian Schipper - The Influence of Heteroatom
Doping of Porous Carbon on the Salt Adsorption
Capacity and Kinetics in CDI (page 88)
Yatian Qu - Characterization of Internal Resistance
for Capacitive Deionization Systems (page 89)
16.20-16.50
Jerome Duval (k) - Dynamics of metal uptake by
biointerfaces (page 81)
Oane Galama - Validity of the Boltzmann equation
to describe Donnan equilibrium at the MembraneSolution Interface (page 82)
Josep Galceran - Recent advances in diffusive
gradients in thin films (DGT). The role of electrostatic
effects and dissolution of metal nanoparticles (page
83)
Louis de Smet - Capacitive Response of PDMScoated IDE Platforms Directly Exposed to Aqueous
Solutions Containing Volatile Organic Compounds
and Salts
Akram Alshawabkeh – Northeastern University, Boston, USA - Electrochemical transformation of contaminants – electrode interface and beyond (page 18)
(Rabobank zaal, chair: Raewyn Town)
14.10-14.50
New materials in CDI / characterization of CDI
Chair: Volker Presser
Lunch
13.00-14.00
General
9
10
10.40-11.10
Mieke Kleijn - Coverage and disruption of phospholipid membranes by oxide nanoparticles (page
105)
Wenfeng Tan - Shape evolution synthesis of
crystalline hematite (α-Fe2O3) nanoparticles using
ascorbic acid and tartaric acid (page 106)
Toshio Sakai - Removal of organic pollutants from
water by TiO2/CnTAB Nanoskeleton (page 107)
Stéphane Daniele - Smart Hybrid Nano-Composite
Devices for Removal of PAH Micro-pollutant from
Wastewaters (page 108)
Romain Dagnelie - Diffusion Of Anthropogenic Organic Matter In Clay Rock (page 100)
Olga L. Gaskova - Uranium migration at nuclear waste management facilities: experimental versus thermodynamic
modeling (page 101)
Munehide Ishiguro - Adsorption of sodium dodecylbenzene
sulfonate in highly humic volcanic ash soil (page 103)
Salini Sasidharan - Coupled Effects of Hydrodynamic and
Solution Chemistry Conditions on Long-Term Nanoparticle
Transport and Deposition in Saturated Porous Media (page
104)
Coffee
Chair: Matthew Suss
Chair: Philippe Behra
Announcements CDI conferences 2015,
2016
Mathijs Janssen - Temperature and size effects on the desalination of water (page 109)
Andreas Haertel - Structural and size effects
on the desalination cycle of water (page 110)
Maarten Biesheuvel - Membrane CDI: definitions, and double layer modeling (page 111)
Dennis Cardoen - Multiphysics simulation of
Membrane CDI for mixed streams (page 112)
Theory of CDI
9.20-10.40
Nanoparticles, materials, effects, transport
Liane Benning – University of Leeds, UK - The Birth and Life Cycle of a Nanoparticle or how to make crystals from ions (page 19)
(Rabobank zaal, chair: Erwin Klumpp)
8.30-9.10
Interaction and processes
Chair: Yasuhisa Adachi
Coffee
8.00
Wednesday
General
Chair: Jerome Duval
13.10-14.10
David Wesolowski – Oak Ridge National Laboratory, USA - The Oxide-Water interface, Neither Oxide Nor Water! (page 20)
(Rabobank zaal, chair: Volker Presser)
Closing ceremony IAP 2014 (Rabobank zaal)
Excursions to Wetsus or Fries Museum. In case you signed up for one of the excursions, please gather outside De Harmonie, near the entrance.
14.50-15.00
15.00
Gang Wang - Ultrasound-assisted Preparation
of Electrospun Carbon Nanofiber/graphene
Composite electrode for CDI (page 126)
Qinghan Meng - CDI of NaCl solution using
activated carbon electrodes in a novel CDI
module (page 127)
Bert van der Wal (k) – Salt removal, water
recovery and energy consumption in
Membrane CDI (page 128)
Chair: Xiaowei Sun
Chair: Liane Benning
Erwin Klumpp - Retention and Remobilization of
Stabilized Silver Nanoparticles in Soils (page 123)
Sondra Klitzke - The role of soil-borne DOC on the
aggregation of synthetic Ag nanoparticles in soils
(page 124)
David Waite - Silver nanoparticle-based water treatment: mechanistic aspects and technology viability (page 125)
Processes in CDI
Nanoparticles (materials, effects, transport)
Matthew Suss (k) - Flow-through electrode
CDI and experimental characterization of
desalination electrodes (page 116)
Jouke Dykstra - Enhanced energy efficiency
in increased discharging voltage Capacitive
Deionization (page 118)
Sung-il Jeon - Seawater Desalination and
Energy Recovery using Flow-electrode
Capacitive Deionization (FCDi) (page 119)
Chair: James Landon
Processes in CDI
14.10-14.50
Raewyn Town - Labilities of aqueous nanoparticulate metal
complexes (page 120)
Yonatan Keren - Wastewater effects on soil-organic
compound interactions, non-typical sorption isotherms and
clay vs. SOM as sorbing phases (page 121)
Liping Weng - Arsenic Adsorption: Effect of pH, Natural
Organic Matter and Oxides Composition (page 122)
Lunch
Jerome Labille - Is solution chemistry responsible for clay
particle mobility through soil pores? (page 113)
Chen Yang - Sorption of tylosin on goethite (page 114)
Philippe Behra - Effect of pyrite interface on silver and
mercury behavior in natural porous media (page 115)
Chair: Mieke Kleijn
12.10-13.10
11.10 -12.10
General
11
Invited plenary lectures
Invited plenaries
13
MON 9.40 - 10.20
Rabobank zaal
Invited plenaries
Reactivity of Iron Nanoparticles: Spectroscopy, Electrochemistry, Kinetics, and
Environmental Implications
Paul G. Tratnyek
Institute of Environmental Health, Oregon Health & Science University, 3181 SW Sam Jackson Park Road, Portland, Oregon 972393098 USA, Email: [email protected], Web: http://www.ebs.ogi.edu/faculty/tratnyek.html
In the early 1990s, permeable reactive barriers (PRBs) containing zero-valent iron (ZVI) emerged as a reliable and cost-effective technology for remediation of groundwater contaminated with chlorinated solvents.
Since then, the range of ZVI applications in treatment processes has expanded to include other classes of
organics (e.g., energetics, pesticides, dioxins, etc.), many metals (As, Cr, Se, etc.), other inorganics (nitrate,
residual chlorine), acid mine drainage, and possibly even some pathogens.
In parallel with the diversification of engineering applications, a large body of scientific literature has developed on many aspects of treatment processes based on ZVI (and other zerovalent metals). This is partly
because granular ZVI in aquatic media has become a favorite model system for investigating many aspects
of interfacial redox processes in the environment. Some of these results are specific to the chemistry of
Fe0, but many are representative of the (bio)geochemistry of ferrous/ferric iron in the environment as a
whole.
In our recent work, we have focused on the role that surface layers of organics, oxides, and sulfides play in
controlling the overall reactivity of granular ZVI with contaminants from the solution phase. Of particular
interest is the coupling between the dynamics of surface layer transformations (e.g., “aging”) and the kinetics of reactions between the particles and solutes. Different aging effects apply to different timescales
- from seconds to months - and we have found important effects across this whole range, often arising in
combinations.
For characterizing interfacial redox processes over diverse timescales, we have found electrochemical methods to be especially valuable. In order to study granular ZVI with its native - or in situ generated - surface
coatings, we use packed powder disk electrodes (PDEs) with electrochemical methods developed for studying passive film effects on corrosion of metallic iron. Using powders consisting of a single phase (e.g.,
high purity micron- or nano-sized ZVI with its native oxide coating), the results obtained by our methods
are usually readily interpretable in terms of established corrosion electrochemistry.
In our most recent work, however, we have expanded the application of this approach to multiphase particulate materials. One example is nano ZVI exposed to sulfide, which creates iron sulfides, which improve
the sequestration of technetium (as the technetium sulfide). Another example is nano ZVI amended with
a range of metals that create authigenic phases by reduction, adsorption, and/or coprecipitation. Interpretation of the data from these systems can be challenging, but some of these challenges can be overcome
by various sorts of modeling or meta-analysis. This presentation will highlight results from several recent
studies using electrochemical methods to characterize interfacial redox processes involving multi-phase
materials containing ZVI. In some cases, it may be necessary to interpret the surface reactivity if the component phases as a product of the overall electrochemical properties of the packed bed as a whole.
Paul Tratnyek is a Professor in the Division of Environmental and Biomolecular Systems and
Institute of Environmental Health, at the Oregon Health & Science University (Portland, OR,
USA). Previously, he served as a National Research Council Postdoctoral Fellow at the U.S.
Environmental Protection Agency Laboratory (1988, Athens, GA, USA), and as a research
associate at the Swiss Federal Institute for Water Resources and Water Pollution Control
(1989-1991, Zurich, Switzerland). His research concerns the physico-chemical processes that
control the fate and effects of environmental substances, including minerals, metals (for
remediation), organics (as contaminants), and nanoparticles (for remediation, as contaminants, and in biomedical applications). He obtained his Ph.D. in Applied Chemistry from the Colorado School of Mines
in 1987 (Golden, CO, USA). Before, he obtained his B.A. (1980) in Biochemistry at the Williams College (Williamstown,
MA, USA).
14
Models of colloids and models for interpretation. A bit of history.
Hans Lyklema
Laboratory of Physical Chemistry and Colloid Science, Wageningen University, Dreijenplein 6, 6703 HB, Wageningen, The Netherlands, E-mail: [email protected]
ment of Agrotechnology and Food Sciences at the Wageningen University. He was Professor
from 1962-1995 in this department, after starting his scientific career as scientific co-worker
and lecturer at the University of Utrecht (1958-1961, Utrecht, The Netherlands). His specialization are colloid and interface science, interfacial electrochemistry, adsorption phenomena,
proteins at interfaces, and electrokinetics. Besides many publications and several books, he
is the author of: “Fundamentals of Interface and Colloid Science”, Vol. I-V. Dr. Lyklema completed the Study Chemistry and Physics (1948-1955), at the State University Utrecht, where
in 1956 he received his Ph.D. degree.
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MON 13.00 - 13.40
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Hans Lyklema is since 1995 Emeritus Professor Physical and Colloid Chemistry in the depart-
Invited plenaries
People like models, intentionally or subconsciously. For professional colloid scientists it is not different.
Over the past century a range of model colloids and a series of model interpretations have been developed
and discarded, many of them leaving relevant contributions to our insight. Some of these model substances are still relevant for IAP, for example insoluble oxides and clay minerals. Similarly, theories for interpreting particle interaction have been polished and extended and subjected to increasingly sophisticated
measuring methods. For illustration, DLVO theory for the stabilization of lyophobic colloids underwent a
number of extensions, its application was widened as a result of the advent of AFM techniques. Looking at
the histories of these developments, it is surprising how much insights, obtained with embryonic theories
and less-sophisticated instrumentation, have left a lasting influence on our knowledge and thinking.
In the presentation some prominent historical illustrations with their present-day extensions will be reviewed.
Perhaps the oldest illustration of utilizing colloids for the understanding of general physical chemistry was
Perrins work of using gamboge mastic colloids and laborious particle counting to assess Avogadro’s number. This work is about a century old. However, the method persisted in that from the nineteen seventies
onward sols of well-defined colloids were used as models for the structure of condensed liquids.
Model substances for the study of colloid stability started with a variety of natural materials, of which
examples can be found in the older editions of Freundlich’s Kapillarchemie, also a century ago. Notable
progress has been made by Kruyt and others of the Utrecht School by using silver iodide as their model
substance. This choice was a lucky strike because silver iodide is chemically rather stable, its charging mechanism by adsorption of charge-determining ions was exemplary, stable sol are relatively easily prepared,
stabilities could eventually be measured and silver iodide electrodes made. A number of insights obtained
with this system are still important but tend to be forgotten, like the inverse coupling of the influence of
indifferent electrolytes on the surface charge and on the sol stability and the origin of ion specificity.
After the silver iodide came the thin liquid films, the homodisperse latices, ludox, and other well-defined
colloids displaying interesting macroscopic phase behaviour. Micro-emulsions deserve special mentioning
because they are thermodynamically stable and homodisperse.
More recently, models with sterically stabilized particles are becoming popular. Till about 1950 no good
theories for these systems existed. Another important branching was stability in media of very low dielectric permittivity.
In real experiments, in addition to trying to achieve maximum experimental information, it is always useful
to subject these data to thermodynamic analysis. For this, mostly well-defined and reproducible data are
needed, but as thermodynamics are phenomenological, their application may help against overinterpretation of models. In some situations surprising new insights can be obtained. A typical elaboration is
obtaining ionic components of charge in electric double layers, that is, splitting the countercharge into the
part by positive adsorption of counterions and the contribution of negative adsorption of co-ions. In the
presentation this option will be elaborated.
TUE 9.00 - 9.40
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Invited plenaries
Should I stay or should I go now:
Assessing electron transfer properties
using mediated electrochemical analysis
of
organic
and
mineral
phases
Michael Sander
Environmental Chemistry, Department of Environmental System Sciences, Swiss Federal Institute of Technology (ETHZ),Switzerland;
email: [email protected]; Webpage: http://www.ibp.ethz.ch/people/sanderm
Electron transfer to and from organic and mineral phases plays a key role in many important biogeochemical redox reactions and in pollutant transformation reactions, in both natural and engineered systems.
As a consequence, considerable research efforts in numerous disciplines have been directed towards characterizing the redox properties and reactivities of major redox active phases, including dissolved and
particulate organic matter (OM), iron-bearing clay minerals, and iron and manganese (oxyhydr-)oxides.
Advances towards a concise understanding of the redox properties were, however, challenged by a lack of
suitable characterization methods. Most studies had to rely indirect wet chemical approaches. For example, the redox states of OM samples were commonly determined by quantifying the number of electrons
transferred from OM samples to added bulk chemical oxidants (e.g., by monitoring the formation of Fe2+
following the addition of a complexed Fe3+ species to the OM). Other studies employed electrochemical
approaches. These, in principle, allow for a more direct assessment of the redox properties and reactivities
of organic and mineral phases: in amperometric measurements, electron transfer to and from the phases
can be directly monitored via reductive and oxidative currents, respectively, between the phases and the
working electrodes of electrochemical cells. In potentiometric measurements, the reduction potential Eh
of the geochemical phases can be monitored via redox electrodes. However, many of the amperometric
and potentiometric measurements in past work showed kinetic artifacts as a result of extremely slow electron transfer and Eh equilibration between the geochemical phases and the working electrodes.
This contribution focuses on mediated electrochemical analysis, a novel approach that we recently developed to characterize redox-active geochemical phases. The first part of the presentation will introduce
mediated electrochemical analysis and present some of the results obtained from applying this approach
to a diverse set of OM samples and to selected Fe-containing minerals. In mediated electrochemical analysis, dissolved redox mediators are used to facilitate electron transfer and Eh-equilibration between the
geochemical phases and the working electrodes in amperometric and potentiometric measurements, respectively (Figure 1). An overview of suitable redox mediators will be given that can be used in measurements over a wide range of reduction potentials from Eh= +0.70 V to –0.54 V (vs. SHE, pH 7). It will be demonstrated how mediated electrochemical reduction and oxidation, two amperometric techniques, can
be used to directly quantify the number of electrons that are transferred to and from organic matter and
Fe-containing phases at defined Eh and pH conditions in electrochemical cells. Several unique advantages
of mediated electrochemical analysis over previous wet chemical approaches will be discussed, including
the possibility to analyze particulate organic and mineral phases and to obtain information on both the
kinetics and thermodynamics of electron transfer to and from these phases. The first part of the presentation will end with an outlook on the broad application domain of mediated electrochemical analysis.
Michael Sander is a senior scientist in Environmental Chemistry at the Swiss Federal Institute
of Technology (Zurich, Switzerland), where he previously held the positions of postdoctoral
associate (2005-2007) and research group leader (2008-2013). The work of his group aims
at providing mechanistic insights into various physicochemical processes in soil and aquatic
environments. The three focus areas of research are environmental analytical electrochemistry and electron transfer reactions, environmental macromolecular chemistry, and the
environmental fate of organic micropollutants. In 2005 he received his Ph.D. in Chemical
& Environmental Engineering from Yale University (New Haven, USA). Before, he obtained
his B.E. (1997) and M.Sc. (2000) in Geoecology at the University of Bayreuth, (Bayreuth,
Germany) and an M.Sc. (2002) in Chemical & Environmental Engineering at Yale University.
16
mediators (M) are used to facilitate attainment of redox equilibrium between the phase and the working electrode of
the electrochemical cell. Mediated amperometric analysis includes mediated electrochemical oxidation and reduction which allow for a direct quantification of the numbers of electrons that can be transferred from and to the sample
at controlled potentials Eh applied to the working electrodes. Mediated potentiometric analysis allows determining
the reduction potential Eh of the samples.
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TUE 9.00 - 9.40
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Figure 1 Schematic of mediated electrochemical analysis of a natural organic matter sample in which soluble redox
Invited plenaries
In the second part of the presentation the unique capabilities of mediated electrochemical analysis will be
highlighted by selected results of two mechanistic laboratory studies on the redox dynamics of dissolved
organic matter (DOM) in temporarily anoxic wetlands. In the first laboratory study, we used mediated
electrochemical analysis to quantify changes in the redox states of four different DOM samples over three
successive cycles of DOM reduction by Shewanella Oneidensis MR-1 under anoxic conditions and subsequent re-oxidation of the reduced DOM by O2 under oxic conditions. Electron transfer to and from the four
DOMs was found to be fully reversible over the three cycles of microbial reduction and O2 re-oxidation.
These findings demonstrate that DOM is a regenerable terminal electron acceptor for anaerobic microbial
respiration in temporarily anoxic wetlands. Mediated potentiometric measurements revealed that the
four tested DOMs accepted electrons over wide reduction potential ranges and that Shewanella Oneidensis MR-1 reduced the DOMs to comparable Eh, suggesting that the extents of microbial DOM reduction
were controlled by system thermodynamics. Some of the implications of reversible and sustainable electron transfer to and from DOM for wetland carbon cycling will be highlighted, including the competitive
suppression of methanogenesis in these systems by using OM instead of CO2 as terminal electron acceptor
in anaerobic microbial respiration. In the second laboratory study, we used mediated electrochemical
analysis to follow the enzymatic oxidation of phenolic moieties in DOM during incubation with phenoloxidases (i.e., laccases). The electrochemical analysis revealed fast, extensive and highly irreversible oxidation of phenolic moieties in DOM by laccase. Furthermore, coupled quantification of DOM oxidation
and O2 reduction by the laccases provided evidence that the initial oxidation of the phenolic moieties in
the DOM is followed by coupling reactions that result in the new-formation of electron donating phenolic
moieties. The implications of enzyme-mediated oxidation of phenolic moieties in DOM will be discussed in
the context of the ‘enzymic latch hypothesis’ that suggests that the activity of phenoloxidases in northern
peatlands is a key factor that controls carbon storage in and CO2 emissions from these systems.
TUE 14.10 - 14.50
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Invited plenaries
Electrochemical transformation of contaminants – electrode interface and beyond
Akram N. Alshawabkeh
Snell Engineering Professor, Northeastern University, Boston, USA
Professor of Civil and Environmental Engineering
PI/Co-Director, PROTECT Center (http://www.northeastern.edu/protect/)
Groundwater contamination is a significant problem in the US, despite three decades of considerable progress
in the cleanup of contaminated sites. The most problematic sites are those with potentially persistent contaminants, including chlorinated solvents, and with hydrogeologic conditions characterized by large spatial heterogeneity or the presence of fractures. Remediation costs are significant; it is estimated that the cost for complete
closure of Superfund facilities that significantly threaten public water supply systems (estimated at 10% of Superfund sites) is at least $110 billion. The US EPA estimated that the cost over the next 30 years to mitigate these
hazards will be more than $209 billion. Inaction may be even more costly, as groundwater contamination can
cause poor health outcomes and result in a greater need for expensive healthcare, taxing our already overburdened system. Our long-term goal is to develop novel, sustainable, solar-powered and environmentally-friendly
technologies for remediation of contaminated groundwater. We use low direct electric currents through electrodes in wells to manipulate groundwater chemistry by electrolysis. Our target contaminants are chlorinated
solvents, specifically trichloroethylene (TCE), but the process is also designed to treat a mixture of contaminants.
Two specific transformation mechanisms are evaluated: electrochemical induced reduction and induced chemical oxidation. Although oxidation occurs at the anode, we demonstrated that chemically-reducing conditions
can be developed in groundwater using iron anodes, and that the pH and redox potential are optimized using
multiple electrodes with controlled current and/or polarity reversal. In contrast to the oxygen-releasing inert
anode, the iron anode generates ferrous species, which regulate the electrolyte to a reducing condition (low
Oxidation-Reduction Potential or ORP value) and favor the reduction of TCE. The system results in up to 99%
dechlorination of TCE with copper foam cathodes. The main products include ethene and ethane; chlorinated
intermediates such as cis-DCE or VC are no longer detected. Furthermore, the ferrous species generated from
the iron anode can reduce and/or co-precipitate certain aqueous contaminants, such as dichromate, selenate
and phosphate. We further evaluated in situ-induced chemical oxidation of TCE in simulated groundwater by
electro-generated H2 and O2 using inert anodes in the presence of Pd and Fe(II). A three-electrode column, one
anode and two cathodes, is employed to automatically develop a specific pH condition in the Pd vicinity and a
natural effluent. By packing Pd/Al2O3 pellets, the column efficiency for TCE oxidation increases with increased
Fe(II) concentration. Oxidation removes 95% of TCE within 80 min, and the product distribution proves that the
degradation pathway shifts from 79% hydrodechlorination in the absence of Fe(II) to 84% oxidation by •OH
in the presence of Fe(II). We demonstrate that in hybrid electrolysis, sulfite at concentrations less than 1 mM
greatly increases TCE oxidation by the production of SO4•-, a strong oxidizing radical, and more •OH. In contrast
to Pd-catalytic hydrodechlorination under reducing conditions, using a hybrid electrolysis and Pd-catalytic oxidation process is advantageous in controlling the fouling caused by reduced sulfur compounds because the in
situ generated ROS, i.e., O2, H2O2 and •OH, can oxidize sulfur. A major advantage of electrochemically-generated
oxidation or reduction is the ability to regulate pH/redox and develop multiple or sequential reactive zones
using multiple electrodes for treatment of a mixture of contaminants within a treatment unit.
Akram Alshawabkeh is a Professor in the department of Civil and Environmental Engineering
at Northeastern University (Boston, USA), at which he previously was assistant Professor
(1997-2002) and associate Professor (2002-2007). He is also the Director of the PROTECT
Center. His fields of expertise are: soil and groundwater remediation, electrokinetic and electrochemical processes, contaminant fate and transport environmental restoration and environmental restoration. In 1994 he received his Ph.D. in Civil and Environmental Engineering
from the Louisiana State University. Before, he obtained his B.E. (1998) in Civil Engineering at
the Yarmouk University (Irbid, Jordan), and his M.Sc. (1990) in Civil Engineering at the Jordan
University of Science and Technology (Irbid, Jordan).
18
The Birth and Life Cycle of a Nanoparticle or how to make crystals from ions
Liane G. Benning
Cohen Geochemistry Laboratory, School of Earth and Environment, University of Leeds, LS2 9JT, UK
References
1. Tobler, D.J., Shaw, S., Benning, L.G. (2009). Geoch. Cosmoch. Acta 144:56-168;
2. Juan Diego Rodríguez-Blanco, Samuel Shaw and Liane G. Benning (2011) Nanoscale 3: 265-271;
3. A. E. S. Van Driessche, L. G. Benning, J. D. Rodriguez-Blanco, M. Ossorio, P. Bots, J. M. García-Ruiz (2012) Science 336:69-72;
4. Dorottya Csákberényi-Malasics, Juan Diego Rodriguez-Blanco, Aleksander Rečnik, Liane G Benning and Mihály Pósfai (2012)
Chem Geol 294-295: 249-258;
5. Pieter Bots,Juan Diego Rodriguez Blanco, Teresa Roncal-Herrero, Sam Shaw, Liane G. Benning (2012) Cryst Gr. Des. 12 (7): 38063814
Liane G. Benning is a Professor in Experimental Biogeochemistry at the University of Leeds
(UK). In 1995 she received her Ph.D. in Aqueous Geochemistry from the Swiss Federal Institute of Technology, (Zurich, Switzerland) after which she worked as a postdoctoral fellow
(1996-1999) in the Department of Geosciences at Pennsylvania State University (State College, USA). Her research addresses geochemical reaction mechanisms at low to hydrothermal
temperatures in inorganic and biologic systems. In this research she uses a variety of conventional and synchtrotron-based laboratory methods, but also some field approaches to study
biogeochemical processes at the molecular level. She obtained her Diploma in Petrology/
Geochemistry (1990) and completed her B.Sc. in Marine Geology/Metamorphic Petrology at
the University of Kiel (1987, Germany).
19
WED 8.30 - 9.10
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I will discuss how using synchrotron scattering and diffraction methods at high temporal resolution allows
now for the nucleation, growth and crystallization pathways for various mineral phases to be evaluated
very precisely. I will address the formation of poorly ordered and nanocrystalline phases (i.e., amorphous
silica [1], amorphous calcium carbonate [2], and nano-crystalline calcium sulphate [3] or iron sulphide [4]
phases) and their crystallization into stable phases (e.g., CaCO3 [5], or CaSO4•2H2O [3]). I will demonstrate
that only through a combination of such in situ solid phase analyses with simultaneous monitoring of
changes in the reacting solvents (e.g., redox, pH, ion concentrations and speciation), and with high-resolution imaging and micro-spectroscopy characterization of the solids can we realistically derive meaningful
mechanism, kinetics and energetics of the relevant reactions.
Invited plenaries
The reactions that control the nucleation, growth and crystallization of mineral phases from solution usually follow a series of complex and often multi-stage reactions that can be slow or extremely fast and that
are thus difficult to assess with conventional techniques. However, novel sample preparation / handling
approaches, combined in situ and time resolved methods (both conventional and synchrotron-based) as
well as new developments in with high-resolution imaging permits now such reactions to be quantified
at more realistic chemical and physical conditions. These can now span and address important environmental problems (i.e., pollutant remediation, carbon capture and storage) but they also help and are applicable to improving various industrial processes (i.e, reducing mineral scale formation; novel functional
materials etc.).
WED 14.10 - 14.50
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The Oxide-Water interface, Neither Oxide Nor Water!
David J. Wesolowski
Chemical Sciences Division, Oak Ridge National Laboratory, Oak Ridge, Tennessee, USA, [email protected]
In the Geochemistry and Interfacial Sciences Group at Oak Ridge National Laboratory, and in collaboration with Argonne National Laboratory and a number of university partners, we integrate neutron and synchrotron X-ray scattering
Invited plenaries
and spectroscopies with multiscale computational models to reveal the structural, dynamic and reactive properties
of aqueous solutions at their interface with minerals. The interfacial region is where all sorption, dissolution, precipitation and surface-catalyzed reactions take place, and the equilibria and kinetics of these processes are profoundly
altered by the unique structural and dynamic properties of both the fluid and the mineral surface in the nanoscale
interfacial region (Figure 1). Intensive investigations, summarized in over 40 publications, of water and brine interactions with model minerals, including calcite (CaCO3), barite (BaSO4), quartz (SiO2), rutile (α-TiO2) and cassiterite (SnO2),
reveal general characteristics of this critical interfacial region, that will be the focus of this presentation. As shown in
Figure 1, the structure of water at the interface with an archetypical metal oxide surface, rutile (110) is very different
from the 3D H-bonding structure of bulk water. The oxygen density at the interface oscillates wildly, both parallel and
perpendicular to the surface, and even the Ti and O atoms of the crystal surface are shifted from their lattice positions (e.g. Zhang et al., 2004, 2007; Predota et al., 2013) in a dynamic manner dependent on the nature of sorbed and
intact or partially dissociated water at the underbonded crystal termination. Our extensive molecular dynamics and
quasielastic neutron scattering studies of water at oxide surfaces (summarized for rutile by Wesolowski et al., 2012)
furthermore demonstrate that interfacial ‘water’ not only exhibits non-bulk-like densities, but also liquid-like diffusional dynamics down to temperatures more than 100 K below the freezing point of bulk water. This is not a metastable
‘supercooling’ effect, but rather a consequence of the observation that interfacial water is not the same substance
as bulk water, at least within a few nanometers of mineral and oxide surfaces. The interfacial fluid structure and dynamics also control the transport and sorption of dissolved species, due to the competing affinities of these solution
constituents for interaction with surface atoms, the highly altered interfacial water, and the hydration spheres around
the dissolved species. Furthermore, the presence of water and its dissociated protons and hydroxyl groups at the surface constitute Nature’s most abundant and ubiquitous ‘capping agents’ that play a major role in the stabilization of
metal oxide nanoparticles, and even influence their crystalline structure (e.g. Wang, et al., 2013). Thus, the interface
is both structurally and dynamically distinct from either the bulk water or the bulk solid, and exhibits its own unique
and important physico-chemical properties that profoundly influence environmental and industrial processes.
Acknowledgement
The bulk of this work was supported by the U.S. Department of Energy, Office of
Science, Division of Chemical Sciences, Geosciences and Biosciences.
References
Predota, M., Machesky, M.L., Wesolowski, D.J., Cummings, P.T., J. Phys. Chem. C
2013, 117, 22852.
Wang, H.-W., Wesolowski, D.J., et al., J. Amer. Chem. Soc. 2013, 135, 6885.
Wesolowski, D.J., et al., Phys. Rev. B 2012, 85, 167401.
Figure 1 Experimentally-validated classical mo-
Zhang, Z., et al., Langmuir 2004, 20, 4954.
lecular dynamics snapshot of the structure of
Zhang, Z., et al., Surf. Sci. 2007, 601, 1129.
aqueous SrCl2 at the rutile (110) crystal surface.
Dr. David J. Wesolowski is a Distinguished R&D Staff Member, Leader of the Geochemistry
and Interfacial Sciences Group, and Director of the Fluid Interface Reactions, Structures and
Transport (FIRST) Center at Oak Ridge National Laboratory (Oak Ridge, USA). His research
interests include: structure and dynamics of interfacial fluids, kinetics and equilibria of ion
adsorption at mineral surfaces, equilibrium thermodynamics of fluid speciation and mineral
solubilities, heterogeneous reaction kinetics, and electrode/electrolyte interactions in nanoporous materials for electrical energy storage and electrocatalysis. He obtained his Ph.D. in
Geochemistry and Mineralogy from the Pennsylvania State University in 1984 (Pennsylvania,
USA).
20
Oral presentations Monday
Monday
21
Reversible trapping of water contaminants on nanoporous carbon electrodes
Mickaël Gineys1*, Sandrine Delpeux - Ouldriane1, Nathalie Cohaut1and François Béguin1
1
CRMD, University – CNRS, 1B Rue de la Férollerie 45 071 Orléans, France
Monday
11.00 - 12.20
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* [email protected]
During the last decade, thanks to the improvement of analytical techniques, a wide variety of micropollutants, like reproductive hormones and pharmaceuticals, have been detected at trace concentrations in
wastewater effluents [1-3].
Activated carbons, presently used in tertiary water treatment, appear as the most prevailing and competing adsorbents for the elimination of pollutants, particularly at low concentration. Indeed, their textural
properties (high surface area ~ 2000 m²/g) and the presence of an accessible porous network, allow high
adsorption rates to be achieved, reaching nearly 100 %, without generation of by–products. However, the
major encountered disadvantage of these materials is their short lifetime due to the regeneration difficulties and expensive processes. Indeed, the high energy consuming conventional methods, essentially based on thermal and chemical treatments, show limited regeneration efficiency. An interesting alternative
consists in the polarization of a carbon electrode with the aim to in - situ regenerate the activated carbon
loaded by the organic pollutants [3-6].
This study is focused on target pollutant representing different families of micropollutants (solvent,
pesticide, hormone, endocrine disruptor, analgesic, anti – inflammatory, antibiotic, neuroleptic …). The
adsorption properties and regeneration efficiency have been investigated on selected pollutants, using
two activated carbon cloths (ACC) with different nanotextural and chemical properties. The reversible
electrochemical desorption was performed through a cathodic or anodic polarization of the adsorbent
depending on the selected pollutant adsorbed. Effects of electrochemical parameters as current polarization, electrolyte composition, concentration and electrode potential on regeneration efficiency have been
explored. HPLC analysis permits us at the same time to follow the pollutant concentration, to quantify
precisely the desorption rates and to observe the stability of targeted pollutant in electrolytic solution
under polarization. To complete this study, the textural properties of carbon adsorbent after adsorption
and desorption have been investigated with the aim to evaluate the proportion of regenerated porosity.
Furthermore the behavior of activated carbon under cathodic polarization has been studied through chemicals and textural characterization techniques.
This type of process should allow the energetic and environmental drawbacks of conventional regeneration methods to be overcome. Such a technique offers great potentialities for the development of soft and
controlled in-situ regeneration processes.
References
1. Huerta – Fontela M., Galceran M.T., Martin – Alonso J., Ventura F., Sci. Total Environment 2008; 397: 31 – 40.
2. Report of the Metropolitan Agencies « Pharmaceuticals in the Water Environment » 2010.
3. Deblonde T., Cossu – Leguille C., Hartemann P., Int. J. of Hyg. and Env. Health 2011; 214: 442 – 448.
4. Conchi O.A., Beguin F., Water Research 2007; 41: 3372 – 3380.
5. Bayram E., Hoda N., Ayranci E., Journal of Hazardous Materials 2009; 168: 1459 – 1466.
6. Delpeux – Ouldriane S., Gineys M., Cohaut N., Beguin F., Extended abstract of the International Carbon Conference, 2013, Rio
de Janeiro.
22
Adsorption kinetics and isotherms of micropollutants onto activated carbon fabric and
felt
Sylvain Masson, Laurence Reinert, Sylvie Guittonneau, Laurent Duclaux
Laboratoire de Chimie Moléculaire et Environnement, Université de Savoie 73376 Le Bourget du Lac Cédex, France
*[email protected]
Proceed on next page
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11.00 - 12.20
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Figure 1 Adsorptio kinetics of each micropollutant on
KIP1200 AC (C0=100 ppm, m=16 mg, V=100 mL).
Monday
A lot of studies have revealed that some organic molecules such as pharmaceutical molecules, solvents,
pesticides, etc. are frequently found in water even after treatment at the exhaust of wastewater treatment
plants. One of the possibilities for removing these so-called micropollutants is the adsorption on activated
carbons. Thus the aim of this work is to better understand the adsorption mechanism of some micropollutants onto activated carbons (ACs) in felt or fabric form.
Eight micropollutants molecules were studied, such as some pharmaceuticals: Carbamazepine (CBZ), Diclofenac (DFN), Ibuprofen (IBP), and Ofloxacin (OFX); an endocrine disruptor: Bisphenol A (BPA), an herbicide: Mecoprop (MCP), a pesticide: Pentachlorophenol (PCP), and a corrosion inhibitor: Benzotriazole
(BTA). Adsorption of Caffeine (CAF) which is an anthropic indicator of pollution in waste water was also
studied. The ACs (KIP1200 fabric and CSV4 felt, from Dacarb, France) were characterized by N2 adsorptiondesorption at 77 K and CO2 adsorption at 273 K, pHpzc (point of zero charge) measurements and acido-basic
titrations (Boehm method). The adsorption kinetics (at C0=100 ppm) and isotherms of each adsorbate
were studied at pH 7.4 in Na2HPO4/KH2PO4 buffered solutions (about 0.04 mol L-1) using UV spectrometry
and HPLC for the analysis of organic molecules in the remaining solution. The kinetics of the single molecule (at C0=10-4 mol L-1) and a mixture of the nine molecules (For each absorbate: C0=1.1×10-5 mol L-1)
were also studied. From the network of the adsorption isotherms at 13, 25 and 40°C, the thermodynamic parameters (isoteric enthalpies, entropies, and Gibbs free energies) were determined. The pore size
distributions of the carbons loaded with micropollutants were determined by DFT simulation from gas
adsorption isotherms, in order to investigate the porosity accessible to the adsorbate.
The activated carbon materials were found to be microporous and mainly ultramicroporous with high specific areas (1560 m²/g for the fabric and 1230 m²/g for the felt). Both contained low amounts of oxygenated
surface groups. The pHpzc of the carbon surface were found to be slightly basic (8.75 for the fabric and 7.85
for the felt), indicating positive surfaces at the studied pH.
Kinetics for shorter time were better simulated by diffusion model (t<400 min) and by pseudo second
model order for longer time. Equilibrium times (Figure 1) were found to depend on the molecule type
following this trend: BTA<CAF<IBP<BPA<MCP<CBZ<PCP<DFN<OFX.
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Monday
The shortest ones were observed for the smaller size molecules such as BTA, CAF, IBP and BPA. The longest
ones were observed for DFN and OFX and PCP (few days). The diffusion in the porous network measured
from kinetics was found to be correlated to the volume and size of the molecules except for PCP. However,
the diffusion was also controlled by the affinity between molecules and carbon.
All the adsorption isotherms were better simulated by Langmuir-Freundlich models except for OFX micropollutant for which the best model is the Langmuir one. For the most part of micropollutants, the affinity
can be explained by pi-pi interactions as the Langmuir-Freundlich coefficients were found almost proportional to the number of unsaturated electrons in the adsorbates both for fabric or felt.
The comparison of the loaded pollutant volume (calculated from the adsorption uptake and the computed
adsorbate volume) with the accessible pore volume (from the pore size distribution of raw ACs) and with
the pore volume of the loaded ACs, enabled to predict the sites of adsorption of the micropollutants. We
concluded that all the studied molecules would be adsorbed in the ultramicropores and that IBP, CBZ, BPA,
CAF and OFX might be located in the supermicropores.
The thermodynamic analysis yielded to values of ΔG°298K typical of a physisorption. Whatever the micropollutants and the adsorbent, the heats of adsorption were found endothermic at low uptake (qe=0.1
mmol/g) suggesting an interaction of the solvent with the micropollutants prior to adsorption. The increase in the positive entropy variation as decreasing the uptake was observed whatever the micropollutants,
suggesting the release of the solvent during the adsorption process at low uptake. As the uptake increased
from 0.1 to 1 mmol/g, the enthalpy variations values became more exothermic, suggesting different adsorption sites as a function of the loading rate. The highest exothermicities at saturation were also related
to a negative variation of the entropies signifying an increase in ordering observed for adsorption of IBP,
MCP and CAF on fabric.
24
Electrochemical reduction of haloacetic acids in a three-dimensional electrochemical
reactor with Pd-GAC particles as fixed filler and Pd-modified carbon paper as cathode
Xu Zhao*, Angzhen Li, Ran Mao, Jiuhui Qu
State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental Sciences, Chinese Academy of
Sciences, Beijing, 100085, P.R. China
*Corresponding author: Tel.: +86-10-62849160; Fax: +86-10-62849160; E-mail: [email protected]
DCAA
MBAA USEPA regulation: HAA <60 (µg/L)
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30
20
Total HAA5 (µ g/L)
HAA (µ g/L)
MCAA
TCAA
DBAA
10
0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 30 32
0
Runtime (d)
Figure 1 HAAs concentration in the effluent of continuous running (initial HAAs concentration: 120 μg/L; current density: 0.3 mA/cm2)
References
1. X. Zhao, A.Z. Li, R. Mao, H.J. Liu, J.H. Qu. Electrochemical removal of haloacetic acids in a three-dimensional electrochemical
reactor with Pd-GAC particles as fixed filler and Pd-modified carbon paper as cathode. Water Res, 2014, 51, 134-143.
2. A.Z. Li, X. Zhao, Y.N. Hou, H.J. Liu, L.Y. Wu, J.H. Qu. The electrocatalytic dechlorination of chloroacetic acids at electrodeposited
Pd/Fe-modified carbon paper electrode. Appl. Catal. B. Environ, 2012, 111-112, 628-635.
25
11.00 - 12.20
Rabobank zaal
60
55
50
45
40
35
30
25
20
15
10
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Monday
Haloacetic acids (HAAs) are important disinfection byproducts in chlorinated water. Electrochemical reduction is found to be the efficient and friendly method for the removal of HAAs. Herein, the reductive removal of haloacetic acids (HAAs) in a three-dimensional electrochemical continuous reactor with
Pd-granular activated carbon (Pd-GAC) particles as fixed filler and Pd-modified carbon paper (Pd-C) as
cathode was studied in this research. Pd-C electrode was prepared from PdCl2 via electrodeposition onto
carbon paper; Pd-GAC particles were prepared by the impregnation of Pd2+ ions onto GAC [1]. Efficient
electrocatalytic reduction of HAAs in this reactor was exhibited. Effects of current density, initial HHAs
concentration, and hydraulic retention time on the HHAs removal were investigated.
Under the current density of 0.3 mA/cm2, HAAs with initial concentration of 120 μg/L were reduced to be
less than 60 μg/L with hydraulic retention time of 20 min. Electron transfer and HAAs diffusion both played
an important role in controlling the electro-reduction process under the conditions of current density less
than 0.6 mA/cm2 with an initial HAAs concentration ranging from 120 to 600 μg/L (Fig. 1). However, the
HAAs diffusion became the primary rate-limiting step when the current density was higher than 0.6 mA/
cm2. The Pd0 and Pd2+ species were detected by X-ray photoelectron spectroscopy [2]. The stability of the
electrochemical reactor in the reduction removal of HAAs was also exhibited.
Developing Efficient Polycation-Clay Sorbents for the Removal of Pharmaceuticals and
Dissolved Organic Matter
Hagay Kohay,1 Avital Izbitsky,1 Itamar Shabtai and Yael MIshael1
Dept. Soil and Water Sci., The Robert Smith Faculty of Agri. Food and Environ, Hebrew University of Jerusalem, Rehovot, Israel
Monday
11.00 - 12.20
Nivo Noord zalen
[email protected] http://departments.agri.huji.ac.il/soils/mishael/
Diclofenac, an anti-inflammatory drug, is one of the most frequently detected pharmaceuticals in water
bodies since its removal by most conventional wastewater treatment plants is low. Recently, we have
developed an efficient sorbent for diclofenac removal based on the adsorption of a specially synthesized
polycation, poly N-methyl 4-vinyl pyridine iodide co styrene (QPVPcS), to montmorillonite. Zeta potential
of the clay (-20 mV) decreased (less negative) with an increase in polymer loading and charge reversal
(+80 mV) was reached at high polymer loadings (0.2 g/g). This positive charge of the composites promotes electrostatic interaction with anionic diclofenac (pKa=4.15). In addition to electrostatic interactions
the polycation has aromatic groups which may induce π–π interaction with the pollutant. To estimate
the contribution of these interaction, diclofenac removal (1 mg/L) by a QPVPcS-clay composite and by a
polycation-clay composite (no aromatic groups), was studied at various ionic strengths (0-100 mM NaCl).
Both composites exhibited complete diclofenac removal at low ionic strength but at higher ionic strengths
its removal by the other composite decreased substantially while its removal by the QPVPcS composite
was slightly compromised. Hence, we suggest that the π–π interaction have a dominant contribution to
diclofenac removal. Electrostatic and π–π interaction can also explain the extremely high affinity of humic
acid to the composite. Surprisingly, the presence of humic acid did not compromise diclofenac removal
but rather increased it suggesting a synergistic effect. The adsorption kinetics of diclofenac and of humic
acid to the composite was substantially faster than to granular active carbon (GAC). The efficiency of diclofenac filtration by GAC and QPVPcS filtration columns in the presence of humic acid and without HA
was studied. Diclofenac removal by the composite filter was slightly higher than by GAC. The removal of
humic acid was significantly higher by the composite filter. In the presence of HA diclofenac removal by the
composite enhanced while its removal by the GAC column was compromised (Figure 1). To conclude, the
removal of diclofenc or of humic acid is more efficient by the developed polymer-clay composite than by
GAC filters. This advantage is more pronounce in a complex system of simultaneous removal.
26
Mineralogical investigations of precipitates obtained by treatment of Cu-rich waste
water by Ferrite process
Soraya Heuss-Aßbichler, Daniel Klapper, Melanie John
Department for Earth and Environmental Sciences, Ludwig-Maximilians Universität München
Theresienstr. 41, 80333 Munich, Germany
[email protected]
11.00 - 12.20
Nivo Noord zalen
27
Monday
Industry wastewater containing heavy metals is generated in various production processes of metalworking (e.g. electroplating). A commonly used removal process is the precipitation of copper as hydroxide.
Another method is the ferrite process: This method involves the addition of Fe2+ ions into the solution at
an elevated temperature. Subsequent alkalinisation and oxidation of the solution causes the formation
of dark brown or black precipitates. Aim of this study was to test the feasibility of the ferrite process for
Cu-rich solutions (up to 10 g/L Cu2+) and to characterize the precipitated material. Various experimental
conditions were performed. The influence of ageing on the precipitates was investigated too.
The results indicate that this process is an effective and economic method to remove copper. After treatment the concentration dropped down to < 0.2 mg/L. Fresh and aged samples were investigated by X-ray
diffraction (XRD). In the fresh sample cuprite (Cu2O) and goethite (α-FeOOH) were identified. After one
hour of ageing, the pattern changed significantly and shows the presence of a cubic structure as the most
dominant phase. The decrease of the cuprite reflexes suggests that all copper is incorporated in the ferrite
structure. The patterns obtained for the samples with longer ageing time are very similar.
FTIR spectroscopy confirms the results from the XRD analysis. In addition it enables the detection of X-ray
amorphous phases. The spectra of the fresh sample show the massive presence of green rust 2 (GR2), a
Fe2+-Fe3+ layered double hydroxyl-sulphate. Within one hour the GR2 bands decrease strongly. After two
days of ageing the GR2 bands disappear, whereas the magnetite bands increase.
Magnetic measurements were performed to determine the Cu-content in the ferrite solid solutions. The
measured Curie temperature, however, corresponds exactly to that of pure magnetite, which is about
580°C.
SEM images of the samples show platy crystals with 20 – 80 nm size and ≈ 5 nm thickness and hence
confirm the formation of GR2 in the fresh samples. Crystals with octahedral shapes and 5 – 50 nm size
were observed as a minor phase. After one hour of ageing GR2 was almost completely transformed in
granular crystals < 20 nm size. At the same time, the quantity of idiomorphic octahedral magnetite crystals
increased. After twenty days the major phase was magnetite with a size of 20 - 80 nm. TEM bright field
images showed that many of the nanocrystals contain characteristic dark cores. Investigations revealed
that they are caused by copper in the metallic state. Furthermore, the results show clearly that iron is
restricted to the prevalent ferrite phase.
In summary, it can be stated that the ferrite process is a simple and inexpensive method to remove Cu2+
ions from wastewaters. The results obtained in this study show clearly, that the postulated formation of
copperferrite by ferrite process cannot be confirmed: They point out that almost no Cu2+ is incorporated
into the ferrite structure. The systematic analysis of the fresh and aged samples shows GR2 as precursor
for magnetite. Note that the size of all precipitated phases is less than 100 nm. Depending on reaction
condition Cu occurs as oxide like cuprite or tenorite. But GR2 may also effect the reduction of Cu2+ to
metallic copper. It occurs as agglomerates of only few nanometer large particles or it is enclosed by pure
magnetite.
Cross-coupling oxidation of bisphenol A during electro-enzymatic oxidative process
He Zhao1, Haitao Li2, Hongbin Cao1, Chenming Liu1
1
Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
2
Beijing Engineering Research Center of Process Pollution Control, Beijing 100190, China
Monday
15.30 - 16.50
Rabobank zaal
Corresponding author, Email: [email protected]
Bisphenol A (BPA) is catalyzed in an electro-enzymatic reactor by a horseradish peroxidase cathode with
the presence of humic acid (HA). During the processes of electrogenerating H2O2 coupling HRP-drived oxidative polymerization on the enzymatic cathode, the removal of BPA can achieve 100% within 5 min reaction (Fig. 1). In initial stage of electro-enzymatic reaction (0-3min), the presence of HA inhibits the removal
rate of BPA, due to competition between BPA self-polymerization and HA self-coupling reaction. However,
in later stage (3-5min), HA significantly promotes the removal of BPA. Results indicate that BPA is oxidized
into self-polymers, and then BPA self-polymers decrease and disappear. Furthermore, HPSEC results (Fig.
2) show molecular weight of (HA+BPA) products (6271.4 Da) are much higher than HA self-coupling products (3267.2 Da) and initial HA (1583.8 Da). Therefore, the BPA self-polymers may be incorporated into HA
matrix, and HA promotes BPA self-polymerization to cross-coupling reaction.
Figure 1 Effect of HA on BPA
removal (immobilized HRP
amount=25 U, I=5 mA).
Figure 2 HPSEC chromatograms of products
in electro-enzymatic systems. (HRP=25 U,
I=15 mA, [BPA]=100 mg/L, [HA]=100 mg/L),
30 min reaction, (i) HA control, (ii) only HA
reaction, (iii) both BPA and HA.
28
Interactions of organic dyes with layered double hydroxides
DARMOGRAI Ganna, MARTIN-GASSIN Gaelle, LAYRAC Geraldine, TICHIT Didier, ZAJAC Jerzy,
PRELOT Benedicte
1
Institut Charles Gerhardt Montpellier, UMR 5253 CNRS-UM2-ENSCM-UM1, Université Montpellier 2,CC 1502, Place Eugène Batail-
lon, 34095 Montpellier Cedex 5, France
E-mail : [email protected]
Orange G (OG), Orange II (OII), Methyl Orange (MO)
The trend in the maximum amount adsorbed was the following MO>>OII≈OG. All ionic species were analyzed (including Na+ as dye counter-ions), in order to elucidate the adsorption mechanism. Sorption tests
were also performed in the presence of such competiting species as common ions (SO42-) or heavy metal
pollutant (Chromium). Nanocalorimetry measurements allowed the thermal effects of the complexation
process to be quantified. The sorption phenomenon was observed to be exothermic in all cases, with the
intensities being a function of the dye structure.
References
1. Rives, V., Layered double hydroxides: present and future. Nova Publishers: 2001.
2. Goh, K.-H.; Lim, T.-T., Influences of co-existing species on the sorption of toxic oxyanions from aqueous solution by nano
crystalline Mg/Al layered double hydroxide. J. Haz. Mat. 180, (1), 401-408.
29
11.00 - 12.20
Nivo Noord zalen
Monday
Layered double hydroxides (LDHs)1 are promising materials for remediation uses due to their lamellar
structure and high exchange capacities. In the literature LDHs are presented as effective adsorbents for various types of pollutants. Nevertheless, only a limited number of studies report the influence of common
anions on the sorption of toxic anions and the influence of the competitive interactions 2. In this work,
synthetic Mg-Al LDHs (([Mg2+1-xAl3+x(OH)2]x+[NO3-x/n •mH2O]x-) with NO3-as an interlayer and exchangeable
anion, were used as adsorbent material. Different characterisation methods were used to investigate the
adsorption mechanisms including UV-Vis Spectroscopy, Ionic HPLC and Isothermal Titration Calorimetry
ITC. Adsorption mechanisms (kinetics and capacity) were assessed for three various organic pollutants,
Methyl Orange, Orange G and Orange II.
Study photocatalytic reactions for pollution remediation by electron ionisation mass
spectrometry
Manuel Nuño, Richard Ball, Chris R. Bowen
Department of Architecture and Civil Engineering, University of Bath, Claverton Down BA2 7AY, UK
Dr Richard Ball: [email protected], 0044 (0)1225 386944
Monday
11.00 - 12.20
Nivo Noord zalen
Prof Chris Bowen: [email protected], 0044 (0) 1225 383660
Mr. Manuel Nuño: [email protected], 0044 7588959162
Since the industrial revolution, an increasing global population demands more resources and energy and it
has led to a greater awareness of pollution and air quality. Photocatalysts can be an effective tool against
greenhouse gases, promoting reactions under a certain light wavelength. This research describes a novel
methodology for the real time in-situ study of solid-gas phase photo-catalytic reactions using different
LED that irradiates in the UV. Photo-catalytic samples consisting of pressed pellets of rutile and anatase
crystalline forms of TiO2 and commercially available photoreactive tile. An ultra-high vacuum right angled
bleed valve allowed a controlled flow of gas from the main reaction chamber at atmospheric pressure to
a mass spectrometer operating at a vacuum of 10-5 mbar. The apparatus and methodology have been demonstrated to provide high sensitivity (ppb). The rate of degradation of NO2 attributed to a photo-catalytic
reaction at the TiO2 surface was sensitive to both crystal structures (anatase or rutile) and wavelength of
irradiation.
30
Keynote
Applications of electrosorption systems for waste water recovery
Xiaowei Sun
CEO, EST Water & Technologies Co., Ltd.
[email protected]
http://www.estpure.com
Monday
Electrosorption Technology has been developed in dealing with the water shortage problem of the world.
It has been found that the electrosorption technology is suitable for the desalination treatment of difficult
waters such as waste water and mine water, due to its robust nature and low energy as well as chemicals
consumptions. Several large scale industrial applications of electrosorption technology were investigated
in this presentation. Various waste waters from chemical plant, steel mill, petrol refinery and coal mines
as well as municipal sewage plant were treated with electrosorption technology and regenerated as fresh
water supplies for corresponding industries, at capacities of 0.6 to 3.5 million gallons per day. Satisfactory continuous operations have been achieved for duration of 2 to 5 years with relatively lower power
consumption and zero chemicals consumption. Studies on the real operations and laboratory experiment
have shown that the deionization effectiveness of electrosorption technology is determined greatly by
electrode material properties and surface oxidation status as well as cell configurations.
11.00 - 12.20
Bentacera zaal
31
Keynote
Continuous performance of double-layer technologies for
water desalination and energy harvesting using flow electrodes
S. Porada1 , D. Weingarth1, H. V. M. Hamelers2, P. M. Biesheuvel2, 4 , V. Presser1, 3
1
INM - Leibniz-Institute for New Materials, Energy Materials Group, 66123 Saarbrücken, Germany
2
Wetsus, Centre of Excellence for Sustainable Water Technology, Oostergoweg 7, 8911 MA Leeuwarden,
3
Saarland University, Campus D2 2, 66123 Saarbrücken, Germany
4
Department of Environmental Technology, Wageningen University, Bornse Weilanden 9, 6708 WG Wageningen, The Netherlands
Monday
11.00 - 12.20
Bentacera zaal
The Netherlands
Email address: [email protected]
Capacitive technologies, such as capacitive deionization1 and energy harvesting based on mixing energy
(“capmix” and “CO2 energy”),2 are characterized by intermittent operation: phases of ion electrosorption
from the water are followed by system regeneration. From a system application point of view, continuous
operation has many advantages, to optimize performance, to simplify system operation, and ultimately
to lower costs. In our study, we investigate as a step towards second generation capacitive technologies
the potential of continuous operation of capacitive deionization and energy harvesting devices, enabled
by carbon flow electrodes using a slurry based on conventional activated carbon powders.3 We show how
the water residence time and mass loading of carbon in the slurry influence system performance. The
efficiency and kinetics of the continuous salt removal process can be improved significantly by optimizing
device operation, without using less common or highly elaborate novel materials. We demonstrate, for
the first time, continuous energy generation via capacitive mixing technology using differences in water
salinity, and differences in gas phase CO2 concentration. Using a novel design of cylindrical ion exchange
membranes serving as flow channel, we establish the ability to continuously extract energy from available
concentration differences that otherwise would remain unused. These results may significantly contribute
to establishing a sustainable energy strategy when implementing energy extracting for sources such as
CO2-emissions from power plants based on fossil fuels.
References
1. S. Porada, R. Zhao, A. van der Wal, V. Presser and P. M. Biesheuvel, Progress in Material Science 2013, 58 1388-1442
2. H. V. M. Hamelers, O. Schaetzle, J. M. Paz-García, P. M. Biesheuvel and C. J. N. Buisman, Environmental Science & Technology Letters, 2014, 1, 31–35.
3. V. Presser, C. R. Dennison, J. Campos, K. W. Knehr, E. C. Kumbur and Y. Gogotsi, Advanced Energy Materials, 2012, 2, 895-902.
32
Keynote
Capacitive deionization based on flowable electrodes
Kelsey B. Hatzell1, Etsuro Iwama2, Anais Ferris2, Barbara Daffos2,
Koki Urita2,4, Theodore Tzedakis3, Fabien Chauvet3, Pierre-Louis Taberna2,
Yury Gogotsi1, and Patrice Simon2
1
Department of Material Science & Engineering and A.J. Drexel Nanomaterials Institute,
Drexel University, 3141 Chestnut Street, Philadelphia, Pennsylvania 19104, USA.
2
CIRIMAT, UMR CNRS 5085, Université Paul Sabatier, Bat. 2R1 118 Route de Narbonne,
31062 Toulouse Cedex 9, France.
3
Laboratoire de Génie Chimique et Electrochimie, Université Paul Sabatier; INPT, UPS, 118 Route de Narbonne, F-31062 Toulouse,
4
Nagasaki University, Department of Applied Chemistry, Faculty of Engineering, 1-14 Bunkyo-machi, Nagaski-shi, Nagasaki 8528521,
France.
Japan.
Speaker Contact: [email protected]
XCT of percolation networks of contact points between carbon active
materials.
33
11.00 - 12.20
Bentacera zaal
Figure 1 (a) Flowing electrode (adsorption occurs at the outlet), and
Monday
Recently, suspension electrodes (‘flowing electrodes’) have emerged as a mode for achieving high capacity
and scalable systems for a range of infrastructure-level challenges (Fig 1a). The core idea behind flowing
electrodes is that the active material (e.g. carbon) can adsorb ions and transport/store electrons to and
from electrodes via percolation networks (Fig 1b). Thus, the physical attributes of these percolation network plays a large role in the performance of these systems (desalination/energy storage/generation/
electrolysis). Furthermore, the dynamic nature of pumping a suspension in order to charge (adsorb ions)
or discharge (desorb ions) charged particles is the defining difference between suspension electrodes and
film electrodes. The physical make-up of the composite suspension electrodes, in terms of weight %, active material size and shape, and rheological principles are critical in order to understand the performance
of a suspension electrode system.
In this talk we highlight the material science aspects of suspension-type electrodes that make it possible
to eke the best possible combination of electrochemical properties in terms of long term cyclability and
electrosorption capacity. Furthermore, capacitive suspension electrodes are introduced as a mode for removing ions from sea or brackish waters. We describe several key aspects toward the design and function
of capacitive suspension electrodes in terms of enhancing the rheological, electrochemical, and kinetic
aspects of these composite-type electrodes.
Keynote
Water desalination by capacitive deionization - Advantages and limitations
E. Avraham*, I. Cohen, M. Noked, Y. Bouhadana, A. Soffer & D. Aurbach
Department of Chemistry, Bar Ilan university, Ramat-Gan 52900 Israel
*E-mail: [email protected]
Monday
11.00 - 12.20
Bentacera zaal
Website: http://www.aurbachlab.com/author/eran#cv
Capacitive deionization may serve as energy efficient method for salt removal from brackish water
(<5000ppm). However, capacitive deionization may have advantages over other competitive desalination
methods. One advantage introduced here is what we call “selective desalination”. Since the salt is electro-adsorbed onto activated porous carbon electrode, the pores could be designed by applying a CVD
process to be in a shape which doubly charged ions like magnesium and calcium ions, which are important
nutrients, could not be electro-adsorbed while sodium ions could be removed selectively from aqueous
solutions. In this way we can retain the magnesium and calcium ions in the feed desalinated water. Another advantage is the possibility to remove boron from water in one stage by exploiting the pH changes
which occur nearby the negatively charges electrode due to surface reactions or water reduction at the
cathode side, in order to transfer boric acid (which is the dominant form of boron contamination in water
at neutral pH) into borate ion which could be electro-adsorbed onto the positively polarized electrode.
We also addressed one of the main limitations of the capacitive ionization method which we call herein
the “Rocking Chair” problem. We are able to calculate the amount of cation and anion adsorbed/desorbed
onto/from the high surface area carbon fiber electrodes as a function of the potential difference applied.
It was revealed that the amount of counter-ions and co-ions electro-adsorbed onto the activated carbon
electrodes are equal from both sides of the PZC at potentials in the range of about 150mV. As a consequence, it was recommended to work at narrow potential domains , i.e. the capacitive deionization cell
should not be completely discharged to 0 volt, but rather to higher potentials (subject for optimization). By
this approach, we were able to demonstrate high charge efficiencies in CDI based desalination processes
but on the account of the salt removal capacities per charge-discharge cycle.
References
1. Eran Avraham,Yaniv Bouhadana,Abraham Soffer and Doron Aurbach. J. Phys. Chem. C, 2008, 112 (19), pp 7385–7389
2. Eran Avraham,Malachi Noked ,Abraham Soffer and Doron Aurbach. U.S. Patent Application Ser. No. 12/477,682 (2009).
3. Eran Avraham,Yaniv Bouhadana,Abraham Soffer and Doron Aurbach. J. Electrochem. Soc., Volume 156, Issue 6, pp. P95-P99
(2009)
4. Eran Avraham,Malachi Noked,Yaniv Bouhadana,Abraham Soffer and Doron Aurbach. J. Electrochem. Soc., Volume 156, Issue 10,
pp. P157-P162 (2009)
5. Eran Avraham,Malachi Noked,Yaniv Bouhadana,Abraham Soffer and Doron Aurbach. Electrochem. Acta. Volume 56, 441 (2010).
34
Keynote
Free Radicals Generating from Catalytic Decomposition
of H2O2: New Strategies and Applications
Xuejing YANG, Xiao-man ZHANG, Pengfei Tian, Jing XU and Yi-fan HAN*
State Key Laboratory of Chemical Engineering, East China University of Science and Technology,
Shanghai 200237, People’s Republic of China
* Corresponding author phone: (+86)21-64251928; fax: (+86)21-64251928
10G
Time (h)
B is p h e n o l A C o n c e n tra tio n (p p m )
d I/d H (a .u .)
Au(3.0 wt% )/S R AC
1.0%
2.0%
3.0%
100
100
80
80
60
60
40
40
20
20
0
0
2
4
6
8
10
12
Figure 1 Time-dependent BPA degradation over Au/
Figure 2 DMPO- trapped EPR spetra of Au/carbon with
Carbon catalysts with different Au loading amount
different Au loading amount
35
13.50 - 15.10
Rabobank zaal
Au(1.5 wt% )/S R AC
0% ,
1.5%
H y d ro g e n P e ro x id e C o n v e rs io n (% )
S R AC
Monday
The increasing worldwide contamination of fresh water systems with various toxic chemicals is becoming
the crucial environmental problem facing humanity [1]. The heterogeneous Fenton process has long been
regarded as a promising alternative for the remediation of refractory compounds in aqueous solution
[2]. However, the poor stability and low efficiency of solid Fenton catalysts hamper the process from
large-scale application. Two strategies have been implemented in the development of solid Fenton-like
catalysts: (1) Supported gold catalysts have proved to outperform the iron-based Fenton catalyst due to
its high stability for the degradation of phenol (Figure 1-2) [3-5]; (2) Redesign Fe-based solid catalysts by
improving the catalytic efficiency in H2O2 decomposition to create OH radicals (Figure 3).
Our studies are mainly focusing on the development of solid Fenton-like catalyst using different preparation methods and raw materials. In particular, the structures of nanoparticles were characterized. By
evaluating the catalytic performance, the kinetics of degradation of persistent organic compounds was
carried out. The structure-performance of those catalysts were established on the basis of characterization results.
In summary, Au/carbon has proved to be effective Au-Fenton catalysts for the degradation of BPA by the
production of OH·. It showed high activity and durability in a broad pH range (3.0-7.0). We tentatively
attribute the generation of ·OH to two factors: (1) Au atoms are polarized or negatively charged on the
carbon surface, which is abundant of dangling bonds; (2) there is few complete basel sites or other sites to
scavenge ·OH. In addition, the unique structural configuration of iron atoms and the reducible electronic
properties of FeOCl are responsible for the excellent activity of Fenton reaction. The high productivity of
OH∙ in this system makes solid Fenton process more practical application for water treatment.
We believe the reported solid Fenton-like system can be an excellent alternatives for rapid purifying drinking water, which may be contaminated with toxic and undegradable organic compounds. Our work can
inspire further study regarding degradation of toxic organic compounds using this simply and stable solid
Fenton system without extra energy input such as photon and electricity.
Monday
E-mail: [email protected] http://skloche.ecust.edu.cn/yfhan/index.html
(a)
-1
1.5
1.0
(B )
13.50 - 15.10
Rabobank zaal
Monday
(b)
-6
In te n s ity (a .u .)
(A)
V O H  1 0 (M S )
2.0
0.5
3420
3450
3480
3510
3540
3570
3600
0.001
Mag netic F ield (G aus s )
0.002
0.003
0.004
0.005
0.006
H 2 O 2 c onc entration (M)
Figure 3. (a) DMPO trapped electron paramagnetic resonance spectra (EPR) at 120 s over FeOCl (A) and conventional Fenton reagent, Fe2+(B); (b) Formation rates of OH· as a function of H2O2 concentration over FeOCl.
References
1. R. P. Schwarzenbach, B. I. Escher, K. Fenner, T. B. Hofstetter, C. A. Johnson, U. von Gunten, B. Wehrli, Science 2006, 313, 10721077.
2. E. Neyens, J. Baeyens, J. Hazard. Mater. 2003, 98, 33-50.
3. X.J. Yang, X.M. Xu, J. Xu, Y.F. Han, J. Am. Chem. Soc 2013, 135, 16058-16061.
4. Y.F. Han, N. Phonthammachai, K. Ramesh, Z. Zhong, T. White, Environ. Sci. Technol. 2007, 42, 908-912.
5. G. Z. Chen, Angew. Chem., Int. Ed. 2010, 49, 5413-5415.
6. S. Navalon, M. de Miguel, R. Martin, M. Alvaro, H. Garcia, J. Am. Chem. Soc 2011, 133, 2218-2226.
7. X.J. Yang, P.F. Tian, C. Zhang, Y.Q. Deng, J. Xu, J. Gong, Y.F. Han, Appl. Catal. B 2013, 134–135, 145-152.
36
Fast degradation in immobilized photocatalytic microreactors
Rob G.H. Lammertink,1 Aura Visan,1 Damon Rafieian,1 Wojciech Ogieglo2
1 University of Twente, Mesa+, Soft matter Fluidics and Interfaces, [email protected], The Netherlands
2 University of Twente, Mesa+, Membrane Science and Technology
Monday
Photocatalytic reactors form an interesting platform for environmental and chemical applications. Despite
the attractive features of photocatalysis, true implementation remains limited. Fundamental understanding of the processes should include mass transport, light distribution and true reaction kinetics. Here we
present a microreactor platform incorporating an immobilized photocatalytic layer in which mass transport and light distribution are accurately desribed. Experimental observations indicate very fast degradation kinetics for a variety of compounds, that are orders of magnitude faster compared to generally reported. The microreactor is modeled by implementing a flux boundary condition into the convection diffusion
equation [1]. The flux boundary condition describes the complete mass transport, light distribution, and
reaction inside the porous catalyst film. This approach is crucial as it allows one to obtain true reaction
kinetics, instead of overall or apparent conversion kinetics. Only with true kinetics it will be possible to
compare catalysts accurately. As such, a Thiele modulus can be defined that includes the light adsorption
characteristics and an internal effectiveness factor is presented that elucidates the relative limitations of
mass and light transport within the photocatalyst layer.
References
1. Visan, A., Rafieian, D., Ogieglo, W., & Lammertink, R. G. H. (2014). Applied Catalysis B: Environmental. Applied Catalysis B: En-
Acknowledgements This work is supported by NanoNextNL, a micro and nanotechnology consortium of the Government of the Netherlands and 130 partners.
37
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vironmental, 150-151, 93–100.
Fast inhibition of direct ammonia oxidation on thermally decomposed iridium oxide
films through a change in local pH
Hanspeter Zöllig, Eberhard Morgenroth, Kai M.Udert*
Eawag, Swiss Federal Institute of Aquatic Science and Technology, Überlandstrasse 133, 8600 Dübendorf, Switzerland
[email protected]
Electrochemical oxidation has gained high attention recently as an efficient method for ammonia removal
from polluted waters. In this study, we tested anodes with thermally decomposed iridium oxide films (TDIROF), which were shown to oxidize free ammonia (NH3) via a direct electron transfer to molecular nitrogen
(N2) and nitrate (NO3-). Unfortunately, TDIROF anodes are rapidly deactivated during ammonia oxidation
which has commonly been attributed to surface poisoning by adsorbed elemental nitrogen (Nads).
In this study, we showed that the fast deactivation of TDIROF not necessarily has to result from surface
poisoning. Instead, we propose that ammonia oxidation and oxygen evolution lead to a pH drop close to
the anode surface resulting in a low availability of the actual reactant, NH3, in the vicinity of the electrode.
In cyclic voltammetry (CV) experiments we showed that TDIROF deactivation can be compensated or even
overcompensated by polarizing the electrode into the hydrogen evolution region (HER) (Figure 1). The
ammonia oxidation peaks of the scans 2 to 5 (A1 solid red line) are higher than the peak in the first scan
(A1 dashed black line). The difference results from the fact that in the scans 2 to 5 the CV has been extended far into the HER compared to the first scan starting from open circuit potential (OCP). We propose
that hydrogen evolution consumes protons and raises the local pH at the potentials in the HER thereby
increasing the amount of NH3 locally. This effect is stronger the longer the potential remains in the HER
and thus depends on the lower return potential (Elower return) (inset Figure 2). Other CV experiments showed
that TDIROF activity for ammonia oxidation could be recovered by letting the electrode rest at OCP for
some time before the next anodic scan. The rest time allowed to balance out the pH value in the Nernst
diffusion layer and the bulk solution, so that the ammonia oxidation peaks for each scan are equal. If TDIROF deactivation would result from surface poisoning by Nads a rest time at OCP would not be sufficient
to reactivate the electrodes. Potentiostatic bulk electrolysis experiments showed that direct ammonia
oxidation at TDIROF continued steadily for 35 hours (Figure 2). If the electrode surface was poisoned one
would expect that the process slows down or stops completely. We conclude that the fast deactivation of
TDIROF is mainly caused by a diffusive inhibition which can be reduced in hydraulically optimized cells. The
inhibition mechanism we propose can be generalized for all electrode materials since acidic conditions
prevail in the Nernst diffusion layer of any anode.
20
A1
HER
10
0
-10
-20
-30
20
ipeak A1
A2
[mA cm-2]
Current density i [mA cm-2]
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* corresponding author: [email protected], phone: +41 58 765 5360, fax: +41 58 765 5389
10
15
5
0
-40
-0.9 -1.1 -1.3 -1.5 -1.7
Elower return [V vs. MSE]
-50
-2
-1.5
-1
-0.5
0
0.5
1
Anode potential Ea [V vs. MSE]
Figure 1 Five consecutive cyclic voltammograms (CV) re-
Figure 2 Total ammonia and nitrate concentrations with
corded in 0.5 M Na2SO4 + 0.125 M (NH4)2SO4 on TDIROF.
respect to transferred charge during potentiostatic elec-
Scan rate: 200 mV s-1, pH = 9.25. Inset: Current density
trolysis of 0.015 M (NH4)2SO4 + 0.11 M Na2SO4 + NaOH.
peak A1 of the 1st (empty bar) and 5th scans (solid bar)
Anode potential: 0.6 V vs. MSE.
in CV with changing lower return potential.
38
Keynote
Carbon Nanofiber and Graphene Composites made by
Electrospinning for Capacitive Deionization
Jieshan Qiu, Qiang Dong, Gang Wang, Bingqing Qian
Carbon Research Laboratory, Liaoning Key Lab for Energy Materials and Chemical Engineering
State Key Lab of Fine Chemical, School of Chemical Engineering
Dalian University of Technology, Dalian, 116024, China.
E-mail address: [email protected] (Jieshan Qiu)
Website address: http://finechem.dlut.edu.cn/carbon/
Monday
Capacitive deionization technology (CDI) is of great potential as an effective approach to removing salt
ions from salted water. One of the challenged issues is the fabrication of high performance electrodes. In
this talk, we will report a novel strategy for fabrication of activated carbon nanofiber/reduced graphene
oxide (ACF/RGO) composite materials by electrospinning, followed by CO2 activation treatment at 800 oC.
The morphology, mechanical property and conductivity of the electrospun ACF/RGO electrode materials
were examined, and the NaCl removal capacity of ACF/RGO electrodes was tuned by changing the graphene ratio. The electrospun nanofibers have two functions: a decorating agent for immobilization of graphene and a substrate to prevent the agglomeration of graphene. The incorprated graphene helps to improve
the conductivity and the pore size distribution of the ACF/RGO electrodes, evidenced by the results that
the ACF/RGO-10 has an electrosorption capacity of 9.2 mg g-1, which is the highest among the ACF/RGO
composites fabricated under the conditions.
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Fig. 1 (a) Photo of ACF/RGO-10, (b)-(d) SEM images of ACF/RGO-10, inset in Fig. 1(c) is the typical TEM image, (e) Side-view SEM image of ACF/RGO-10, and (f) SEM image of ACF
Fig. 2 (a) The NaCl electrosorption capacity of ACF, RGO and ACF/RGO-10 electrodes vs. time in CDI; (b) the desalination capacity of ACF, RGO and ACF/RGO-X (X stands for the weight ratio of RGO in the electrodes), for which the test
conditions are Vcell :1.2 V, VNaCl:30 mL, and C0:400 mg L-1
39
Effect of pore size and its dispersity of porous carbon on capacitive deionization
Volker Presser1,2 and Slawomir Porada1
1 INM – Leibniz Institute for New Materials, Saarbrücken, Germany, http://www.inm-gmbh.de
2 Saarland University, Saarbrücken, Germany, www.uni-saarland.de
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mail: [email protected]
Porous carbons continue to dominate the field of capacitive deionization (CDI) for good reasons: it is an
abundantly available resource with low or moderate costs yielding a high CDI performance. All electrodes
used for CDI are porous at various length levels and even per se non-porous carbons (e.g., carbon nanotubes) show a large pore volume comprised from the space between particles; thus, it is of high importance to consider the total pore volume (inter- and intraparticle porosity) and its impact on the resulting
CDI performance. In particular, we will review the importance of porosity measurements, the pitfalls of
applying deconvolution algorithms to conventional sorption analysis data, and novel strategies to develop
predictive tools for CDI sorption capacities and kinetics.
Recently, studies on microporous carbon gave convincing evidence that pores smaller than 2 nm are of
high importance for the electroadsorption capacity of salt in CDI electrodes.[1] This has been a change of
paradigm: before, it was believed that rather larger pores, so called mesopores (2-20 nm), are beneficial
for CDI capacity.[2] New results by us, employing model carbons with precisely tuned porosity, however, show that micropores contribute to much higher degree to the salt sorption capacity compared to
mesopores.[3] We used our novel nanoporous carbons to establish a predictive tool: based on cumulative
pore size distributions, we were able to predict at 1.2 V and 5 mM salt concentration the salt electrosorption capacity of a large array of carbon materials in the literature. In a second step we also used a
two-dimensional transport model to predict the sorption kinetics and to evaluate the optimum electrode
material compaction level for salt electrosorption.
References
1. Porada, S., et al., Water Desalination Using Capacitive Deionization with Microporous Carbon Electrodes. ACS Applied Materials
& Interfaces, 2012. 4(3): p. 1194-1199.
2. Y ang, K.-L., et al., Electrosorption of Ions from Aqueous Solutions by Carbon Aerogel: An Electrical Double-Layer Model. Langmuir, 2001. 17(6): p. 1961-1969.
3. P
orada, S., et al., Direct Prediction of the Desalination Performance of Porous Carbon Electrodes for Capacitive Deionization.
Energy & Environmental Science, 2013. 6(12): p. 3700 - 3712.
40
Preparation of a MnO2/Carbon Composite Electrode for Electrosorptive Removal of
Heavy Metal from Water
C.Z. Hu, F.Y. Liu, H.C. Lan, H.J. Liu*, J.H. Qu
Research Center for Eco-Environmental Sciences, Chinese Academy of Sciences, Beijing 100085, China
E-mail of corresponding author: [email protected]
E-mail of the first author: [email protected]
1. J. Yang, L. Zou, H.H. Song, Z.P. Hao, Desalination 276 (2011) 199-206.
2. S.G. Wang, W.X. Gong, X.W. Liu, Y.W. Yao, B.Y. Gao, Q.Y. Yue, Sep. Purif. Technol. 58 (2007) 17–23.
3. M.A. Salam, Colloids and Surfaces A: Physicochem. Eng. Aspects 419 (2013) 69–79.
41
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References
Monday
It has been believed that the physical properties and the structure of electrode materials dominate its
electrosorptive performance. Manganese dioxide (MnO2) has been extensively studied as an effective
absorbent to remove heavy metals from water. Meanwhile, MnO2 is a promising electrode material for
electrochemical supercapacitors because of its high specific capacitance, good cycle stability, low cost,
eco-friendly nature and abound availability. MnO2/carbon composite materials show great potential as
electrodes for electrosorptive removal of contaminant ions from water. Yang et al.[1] synthesised MnO2/
nanoporous carbon composites and successfully used them as electrode in capacitive deionization technology. In addition, MnO2/carbon materials composite showed great adsorption ability to remove heavy
metal ions from waste water [2, 3]. Althrough MnO2 is an effective absorbent for many metal ions and a
promising electrode material for electrochemical supercapacitors, no previous study combines the two
properties and uses it as electrode to remove metal ions by electrosorption process.
In the present study, a simple and cost-effective electroplating approach was used to directly deposit a
thin MnO2 layer on the surface of carbon cloth (CC). Morphology, structure, and capacitive properties of
the prepared MnO2/CC electrode were characterized. On the basis of the materials characterization, we
evaluated the electrosorptive performance of the MnO2/CC electrode on Cu2+ and Pb2+ removal. The scanning electron microscope images clearly showed the film of nano MnO2 clusters on CC surface. With increasing deposition time, the thickness of nano clusters gradually increased. An XRD pattern for the MnO2/
CC electrode indicated a long-range disorder of MnO2 in these composites. Electrochemical characteristics
of the MnO2 /CC electrodes prepared for different deposition periods were evaluated by using cyclic voltammetry (CV). The voltammetric current response, and consequently the capacitance of the coating,
increased substantially with increase in deposition time from 500s up to 7200s. The capacitance, however,
it calculated that deposition time of 1000s was optimum for achieving maximum capacitance and the
capacitance was as high as 380 F/g. The MnO2/CC electrodes showed high efficiency on electrosorptive
removal of Cu2+ and Pb2+ from water. Voltage, pH, and the amount of loading MnO2 significantly influenced
the electrosorption performance in Cu2+ and Pb2+ removal.
Zinc oxide nanorods coated carbon electrodes for improved energy efficient capacitive
desalination of brackish water
Karthik Laxman, Myo Tay Zar Myint and Joydeep Dutta*
Chair in Nanotechnology, Water Research Center, Sultan Qaboos University, PO Box 33, Al-Khoud 123, Sultanate of Oman
*
Corresponding author. Tel: +968 2414 3794/3266; Fax: +968 2441 3532
Monday
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E-mail: [email protected]
Capacitive deionization (CDI) with its low energy consumption and capital costs accompanied with a smaller footprint and portability is catching recent attention worldwide, especially for desalting brackish water.
It works on the principle of electric field mediated ion adsorption in the electrical double layer (EDL) formed at the electrode surface upon the application of an external potential. Symmetrically assembled activated carbon cloth (ACC) electrodes having a high surface area can increase the ion adsorption capacity,
increasing the salt removal efficiency of the system. By coating the ACC surface with a dielectric material
like zinc oxide nanorods (ZnO)1, we were able to increase charge efficiency of the composite electrode by
20%, attributed to increase in capacitance of the electrode. Uniform electric field distribution at the ZnO
nanorods surface increased the ion adsorption and desorption rate at the electrode surface, increasing
the salt removal efficiency by 45%. Faster ion transfer rates also contributed to reducing the desalination
and regeneration times by an average of more than 50%, leading to a net power consumption of less than
25 mW per adsorption cycle. The reduction in regeneration time led to a reduction in the overall water
wastage during the process thus improving the recovery rate. The electrodes were characterized for active
surface area, capacitance from cyclic voltammetry curves and theoretical assessment of surface area utilization and magnitude of electric field force acting on an ion of unit charge for an applied potential. Some
results on larger electrode sized capacitive desalination prototype will also be discussed.
References
1. S Baruah, J Dutta, Science and Technology of Advanced Materials 10 (2009), 013001; MTZ Myint, J Dutta, Desalination 305 (2012)
24-30
42
Geochemical and microbiological characteristics during in situ chemical oxidation and
in situ bioremediation at a diesel contaminated site
Nora B. Sutton1*, Mariusz Kalisz2, Janusz Krupanek2, Jan Marek3, Tim Grotenhuis1, Hauke Smidt4,
Jasperien de Weert5, Huub H.M. Rijnaarts1, Pauline van Gaans5, Thomas Keijzer5
1
Environmental Technology, Wageningen University, The Netherlands
2
Institute for Ecology of Industrial Areas, Poland
3
POWIZ Sp. z.o.o Przedsiębiorstwo Oczyszczania Wód i Ziemi, Poland
4
Laboratory of Microbiology, Wageningen University, The Netherlands
5
Soil and Groundwater Systems, Deltares, The Netherlands
*
[email protected]
Table 1 On-line extraction steps
250
Iron
200
30
150
20
100
10
50
0
0
Iron (mg kg-1)
Sulfur (mg kg-1)
300
Sulfur
40
40
250
200
30
20
0
80
80
60
60
40
40
20
20
CaCl 2
1500
H2O2
HNO3
Time (s)
2
2% H2O2
Organic Matter
3
0.45 M HNO3
Easily extractable sulfides, oxi-
4
3 M HCl
des and carbonates
Amorphous and crystalline Fe
Iron (mg kg-1)
100
1000
clays and organic matter
rals, feldspars and pyrite
0
500
Reversibly bound cations on
and Mn hydroxides, clay mine-
100
0
0.01 M CaCl2
100
50
0
Targeted soil Component
150
10
Sulfur (mg kg-1)
C
Iron (mg kg-1)
300
Sulfur (mg kg-1)
B 50
1
Extraction solution
0
2500
2000
HCl
Figure 1 On-line sequential extraction of soil samples
Figure 2 Changes in SOM as measured by TGA analysis. To-
from before treatment (A), after the first persulfate in-
tal weight loss is given on the left axis. On the right axis the
jection (B), and at the end of the experiment period
derivative of weight loss with respect to temperature rela-
(C) for sulfur (black line, left axis) and iron (gray line,
tive to the total weight loss is given to allow comparison of
right axis).
the relative contribution of different soil components.
43
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A50
Monday
While in situ chemical oxidation with persulfate has seen wide commercial application, investigations into
the impacts on groundwater characteristics, microbial communities and soil structure are limited. To better understand the interactions of persulfate with the subsurface and determine the compatibility with
further bioremediation, a pilot scale treatment at a diesel contaminated location was performed consisting of two persulfate injection events followed by a single nutrient amendment. Groundwater parameters
measured throughout the 225 day experiment showed a significant decrease in pH and an increase in
dissolved diesel and organic carbon within the treatment area. Molecular analysis of the microbial community size (16S rRNA gene) and alkane degradation capacity (alkB gene) by qPCR indicated a significant,
yet temporary impact. Analysis of soil samples with sequential extraction (Table 1) showed irreversible oxidation of metal sulfides (Figure 1), thereby changing subsurface mineralogy and potentially mobilizing Fe,
Cu, Pb, and Zn. Additionally, irreversible changes to soil organic matter quality were measured (Figure 2).
Together, these results give insight into persulfate application in terms of temporal and structural effects
on soil structure, microbiology, and risks.
Removal of MTBE from groundwater by adsorption and catalyzed ozonation
ir. L. Fassotte-Harmsen, dr. ir. H. Bruning, prof. dr. ir. W.H. Rulkens, prof. dr. ir. H.H.M. Rijnaarts
Wetsus / Wageningen University, The Netherlands
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[email protected], www.wetsus.nl, www.wageningenur.nl
Groundwater contamination with methyl tertiary butyl ether (MTBE, a petrol originated additive) forms a
threat to drinking water supply from groundwater, mainly because of its bad taste and odour. Hydrophobic
zeolites were shown to be effective for removal of MTBE from water at low concentrations (0-100 µg/L).
The zeolite can be regenerated using advanced oxidation processes. By combining adsorption and oxidation, oxidation can take place at elevated concentration levels compared to oxidation in the bulk water
phase. A second advantage is the selective adsorption of MTBE excluding natural organic matter from the
oxidation. Moreover, catalytic activity of the zeolites may enhance the oxidation process.
In this research the combination of adsorption and ozonation was tested for a high silica ZSM-5 type
zeolite. Main objectives are to find optimal conditions for regeneration of zeolite, and to investigate long
term performance. This was tested by batch ozonation experiments. Most regeneration experiments were
performed with powdered adsorbent and long term performance was investigated with zeolite beads. The
zeolite based process was compared with a granular activated carbon (GAC) based process.
Ozonation experiments showed that the zeolite acts as a strong catalyst in the ozonation of MTBE. In
presence of activated carbon MTBE was oxidised at lower rate and less ozone was consumed. Addition of
hydrogen peroxide resulted in higher ozone consumption without enhancing MTBE ozonation. So radicals
formed in the bulk liquid may not be able to reach MTBE adsorbed on zeolite. pH did not have a significant effect on MTBE oxidation. MTBE oxidation increased at a pH of 13, but this pH damaged the zeolite
structure. Oxidation rate on zeolite beads was faster than on zeolite powder. At typical groundwater temperature (10°C) MTBE ozonation was faster than at room temperature, due to better solubility of ozone
at low temperature.
In long term experiments zeolite and activated carbon were reused for several cycles of MTBE adsorption
and ozonation. Zeolite was used for 8 cycles, without observing a negative trend in the oxidation rate (Figure 1) or MTBE adsorption capacity. Decrease in oxidation rate (Figure 1) and MTBE adsorption capacity
were observed for GAC within 5 cycles. So GAC is less suitable in combination with ozonation.
Figure 1 Effect of regeneration cycle on MTBE ozonation rate (presented as kinetic oxidation constants) for zeolite and GAC
44
An Innovative 2-Stage Process for the Recovery of Phosphorus and Recycling of Ferric
from Ferric Sludges Generated in Water and Wastewater Treatment
E. Mejia Likosova1, J. Keller1, Y. Poussade2, S. Freguia1
Advanced Water Management Centre, Gehrmann Labs, Level 6, The University of Queensland, St. Lucia, QLD, 4072, Australia
1
2
Veolia Water Australia, Level 15, 127 Creek Street, Brisbane, QLD, Australia
[email protected]
Make-up Sulfide solution
• S2-= 0.4±0.2g
• pH ~ 11
Acid addition
•
•
•
Stage I
PO43- recovered in solution
(in case of FePO4 sludge)
• 0.3±0.2 g P L-1
• VSS: 0.3±0.1 g
• pH ~ 4
Real Ferric sludge
Total Fe: 0.9±0.1 g
VSS: 1.8±0.3 g
Controlled at pH 4
~3 g NaCl
•
•
•
•
VSS free
Soluble iron
solution ready
for reuse
(<10 mg VSS)
Sulfide solution
• S2-= 0.4±0.2g
• pH > 10.5
eReal FeS sludge
S/Fe molar ratio: 1.5
Total Fe: 0.9±0.1 g
VSS: 1.5±0.5 g
pH ~6 after dilution
with NaCl stream
•
•
•
V
e-
Fe2+/Fe3+
S0
HS-
S0
FeS Fe2++ S2-
Soluble Fe solution
Total Fe: 0.56±0.05 g
VSS: 0.5±0.1 g
pH < 2
ANODE
MVCEM
CATHODE
Stage II
RO water
pH ~ 7
VSS: 0.5±0.1 g
Figure 1 Two-Stage Iron and phosphorus recovery process
45
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RESULTS AND CONCLUSIONS
The process has been implemented at lab-scale with several consecutive runs being performed successfully
whereby real FeS precipitate formed in Stage I (~3 g Fe/L) is fed to the anode of Stage II and the cathode
effluent from Stage II used to form FeS in Stage I. Up to 70% P was recovered in solution in Stage I at pH
4 and 1.5 S:Fe molar ratio. Additionally, up to 83% of the volatile suspended solids (VSS, mainly organics)
co-precipitated with the FeS particles. After feeding the FeS-VSS suspension to the anode of Stage II, up
to 60% Fe and 50% S were recovered in the anodic and cathodic solutions respectively. The VSS contained
in the anodic solution were easily removed by gravity settling. Peak current densities were 9.5 ± 4.2 A
m-2, while power requirements were 2.4 ± 0.5 kWh/kg Fe, which offers a significant economic advantage
compared to the purchase of ferric chemicals. The demonstration of this process concept is an important
stepping-stone towards a full-scale implementation in both drinking water and wastewater industries.
Monday
ABSTRACT
Ferric salts are used extensively in wastewater treatment to precipitate P, and as coagulant in water
treatment. In all cases, large amounts of ferric sludge are produced. The ongoing chemical supply and
sludge disposal represent a major operating cost to the water industry. A novel 2-stage process for Fe and
P recovery from ferric phosphate sludge has been developed to enable the on-site recycling of ferric for
such applications. In Stage I, PO4 is released in solution after the addition of a sulfide solution to initiate
FeS precipitation. In Stage II, FeS is electrochemically oxidised to elemental sulfur that is deposited on the
anode and generates a low-pH Fe solution for reuse. Simultaneously the cathodic reduction of sulfur forms
sulfide, which can be reused in Stage I to create a fully integrated process (Figure 1).
Heterogeneous Fenton oxidation of catechol and 4-chlorocatechol catalyzed by nanomagnetite: role of the interface reaction
He Jie a,b, Yang Xiaofang a, Wang Dongsheng a,*
a
Research Center for Eco Environmental Sciences, CAS, Beijing 100085, China
b
University of Chinese Academy of Sciences, Beijing 100049, China
E-mail:
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*Corresponding auther. [email protected];
He Jie, [email protected]; Yang Xiaofang, [email protected]
The nano-magnetite catalyzed Fenton oxidation of catechol and 4-chlorocatechol in aqueous solution was
investigated. The synthesized nano-magnetite (MNPs) was used as catalyst and characterized with various
methods. Batch experiments showed that only about 10 % of catechol or 4-chlorocatechol adsorbed onto
nano-magnetite, however almost all the parent compound could be removed within 2 h after addition
of H2O2. The oxidation curves of catechol and 4-chlorocatechol were best fitted by the pseudo-first order
and pseudo-third order kinetic model, respectively. The reduce of pH and the analysis of oxidation intermediates and products measured by ion chromatography (IC) and GC/MS suggested the generation of
carboxyl acids. The electron spin resonance (ESR) spectroscopy showed that the reactive oxygen species
(ROS) were •OH and oxygen-centered radicals in both oxidation systems, and carbon-centered radicals
were only detected during the oxidation of catechol. The low iron leaching indicated a heterogeneous reaction mechanism. Moreover, in situ attenuated total reflection FTIR (ATR-FTIR) spectroscopy showed the
adsorbed catechol or 4-chlorocatechol remained at the surface during oxidation, implying an Eley-Rideal
mechanism. Accordingly, a shematic diagram of oxidation mechanism of catechol or 4-chlorocatechol in
the MNPs/H2O2 system was proposed.
Figure 1 ATR-FTIR spectra of catechol (right) and 4-chlorocatechol (left). [H2O2]0= 0.05M; pH=6.5;
[catechol]0=[4-chlorocatechol]0= 1 mM.
46
Synthesis and complexation properties of new polyvinyl alcohol (PVA)-based chelating
polymers
MULLER Julien, PRELOT Benedicte, GENESTE Amine, ROBIN Jean-Jacques, ZAJAC Jerzy, and MONGE
Sophie
Institut Charles Gerhardt Montpellier, UMR 5253 CNRS-UM2-ENSCM-UM1, Université Montpellier 2,
CC 1502, Place Eugène Bataillon, 34095 Montpellier Cedex 5, France
Sorption tests of these metal cations were investigated in a multi-component solution occurring from
industrial effluent based on Ca(II) and Mn(II) ions. Results achieved were similar to that obtained in water. Finally, the modification of different parameters, including EDTA rates and polymer chain lengths,
was assessed and complexation tests have allowed us to determine the optimal structure for water
decontamination.
47
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Figure 1 ITC data describing the interactions of Co(II) cations with PVA(EDTA)15%
Monday
A series of water-soluble polyvinyl alcohol (PVA)-based chelating polymers with various proportions of
sorption sites were obtained. They were synthesized by reaction between PVA and ethylenediaminetetraacetic acid (EDTA) via Mitsunobu’s reaction in order to afford PVA(ETA). Various functionalisation rates
were reached (5, 10 and 15% in EDTA) and resulting copolymers were able to be tested for ion selective
liquid-liquid extraction. Different characterisation methods were used to investigate complexation properties of PVA(EDTA) including High-Performance Liquid Chromatography (IC for Ionic Chromatography), Isotherm Titration Calorimetry ITC and polarography. Performances of PVA(EDTA)15% were assessed in presence of several metal cations as Co(II), Ni(II), Pb(II), Zn(II) and Cu(II) in aqueous solution. Selectivity could be
established between given metallic cations as function of their affinity towards PVA(EDTA)15%. Moreover,
great sorption capacities can be reached in the case of some cations. For example, the maximum sorption quantity for Co(II) is 1.4 mmol.g-1 which is comparable to resins commonly used in decontamination
process. Nanocalorimetry measurements allowed the knowledge of thermal effects of the complexation
process. It is possible to note an exothermic sorption phenomenon in the case of Co(II) (Figure 1).
Sorption tests of these metal cations were investigated in a multi-component solution occurring from
industrial effluent based on Ca(II) and Mn(II) ions. Results achieved were similar to that obtained in water.
Finally, the modification of different parameters, including EDTA rates and polymer chain lengths, was
assessed and complexation tests have allowed us to determine the optimal structure for water decontamination.
Non linear optical tools to study ions remediation processes
Gaelle Martin-Gassin,1 Pierre-Marie Gassin2
1) Montpellier Charles Gerhardt Institute, France , [email protected]
Monday
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Nivo Noord zalen
2) Institute for Separative Chemistry of Marcoule , France , [email protected]
Water pollution has a large impact on the everyday life of people. This topic requires of combining all
possible skills to understand better fundamental mechanisms and improve the remediation processes.
This multidisciplinary work at frontier between physical methodology, organic chemistry and physical
chemistry of solutions gives a new approach to understand the mechanisms of depollution in order to
optimize them. Solvent extraction, discussed here, is one of the most common and widely used processes
to separate and concentrate substances in solution. The phase transfer reaction occurring at the liquid-liquid interface is often facilitated by the formation of complex species using oil-soluble ligands, also called
extractants. These extractants have some slight amphiphilic features and the complexation will affect their
interfacial properties. Today, it is considered essential to understand the organization of these extracting
molecular compounds at the interface both in absence and during the extraction process in order to get a
clear molecular picture of the extraction phenomena.
Figure 1 Remediation process by complexation at liquid interface.
Such a study often starts with an initial stage where the complexation reaction is investigated, and this
may be performed at the air-water interface, like in the study [1] presented here. A molecular organic
chromophore, PalmitateLuciferin, has been synthesized for studying ion complexation at the air-water
interface using Second Harmonic Generation (SHG). The SHG technique, with a high surface sensitivity,
is one on the most adapted technique to study the active interfacial behavior at the molecular scale. The
molecule PalmitateLuciferin, was designed through the addition of a long hydrophobic palmitoyl alkyl
chain to the aromatic π- electron system of Luciferin. We first demonstrate that this organic chromophore
is a potential candidate for SHG studies of ion complexation with the measurement of its first hyperpolarizability in aqueous solutions by Hyper Rayleigh Scattering (HRS) with and without calcium ions. Then, we
characterize the PalmitateLuciferin surfactant properties at the air-water interface combining surface tension measurements with a surface SHG study and Brewster angle imaging. These results allow us to build
a molecular description of the chromophore at the interface and observe its molecular re-organization
during the monolayer compression leading to the formation of aggregates. Finally, we show that the initial
goal of the designing work is achieved since PalmitateLuciferin indeed exhibits a higher SHG response in
the presence of calcium ions in the aqueous sub-phase as expected.
References
1. Martin-Gassin G., Gassin P.-M., Arrachart G., Benichou E., Diat O., Pellet-Rostaing S., Brevet P.F. Molecule Design for Liquid Interfaces Studies by Second Harmonic Generation: the Palmitoylluciferin , Journal of Physical Chemistry C,. 2012, 116, 7450−7456.
48
Preparation of γ-AlOOH loaded-zeolites and characteristics for phosphate adsorption
Panyue Zhang, Duo Zhang, Jie Ye
College of Environmental Science and Engineering, Beijing Forestry University, Beijing 100083, China
Email address: [email protected], [email protected], [email protected] Monday
Phosphorus is one of the most important elements leading to water eutrophication, meanwhile, phosphorus is one of the non-renewable available resources. People have paid more attention to the removal
and recycling of phosphorus in wastewater treatment. In this study, one kind of modified zeolites, zeolites
loaded with γ-AlOOH (γ-AlOOH-Z), was prepared with precipitation of AlCl3 and used to adsorb phosphate
from the wastewater. Under the optimal preparation conditions, aluminum was loaded on zeolites (with
a particle size of 100-120 mesh) with a loading amount of 116.1 mg/g, and the phosphate adsorption
capacity of γ-AlOOH-Z reached 16.16 mg/g, which increased by 87.5% compared with that of the natural
zeolites. XRD patterns showed that pure γ-AlOOH were successfully loaded on the natural zeolites, and
the preparation conditions including temperature, pH, time significantly affected the loading of γ-AlOOH
and species of aluminum, further impacted the phosphate adsorption. Electrostatic interaction and ligand
exchange were the main mechanisms of phosphate adsorption onto γ-AlOOH-Z, and the ligand exchang
between surface hydroxies and phosphate ions was the main one. Five cycles of adsorption-desorption
process showed that desorption efficiency maintained at about 95%.
15.30 - 16.50
Nivo Noord zalen
Figure 1 X-ray diffraction patterns of γ-AlOOH-Z under the optimal
preparation conditions and natural zeolite
References
1. Chen X Y, Huh H S, Lee S W. Hydrothermal synthesis of boehmite (γ-AlOOH) nanoplatelets and nanowires: pH-controlled morphologies. Nanotechnology, 2007, 18(28): 285608-285612.
49
Removal efficiency of high concentration waste water using Capacitive Deionization
Process
Jihun Kim, Sunkyung You, Hanjoo Kim, Heejoong Kim*, Bokje Bae**, Yunkwon Kim***, Soogil Park****,
PureEchem Co., Ltd, *Hansu Technical Service Co., Ltd, **HSP Co., Ltd, ***K-water institute, ****Chungbuk National University, Republic
of Korea
The volume of usable fresh water has been decreasing globally due to pollutions of river and underground
waters. The pollution of underground water, resulted from phosphate and nitrate ions, eutrophicated. For
the prevention of these problems, the need to disposal of nitrate and phosphate ion is currently growing
day by day. This study is to confirm ion adsorption properties of nitrate ions and phosphate ion in high
concentrate-synthetic waste water by using CDI(Capacitive Deionization) process.
CDI cell was fabricated to confirm ion adsorption properties, and synthetic waste water made of 5,000ppm
NH4-N, 4,000ppm NO3-N, 3,000ppm PO4-P is used. In experiment method, batch type of charging 1 minute
and discharging 3 minutes proceeded after inflow of synthetic waste water into CDI cell. Charging and
discharging as 1 cycle, 40 cycles proceeded, and then treated waste water which drained out from discharge process analyzed with sampling.
This study researched on ion adsorption properties for elimination of nitrate and phosphate ion in high
concentrate-synthetic waste water using CDI process. As a result, it was confirmed that NH4-N, NO3-N,
PO4-P are respectively 79.61%, 72.10%, 73.97% adsorbed.
NH4-N
NO3-N
PO4-P
5000
Concentration(mg/L)
Monday
15.30 - 16.50
Bentacera zaal
[email protected], www.pureechem.com
4000
3000
2000
1000
0
0
10
20
30
40
Cycle
Figure 1 Variation of NH4-N, NO3-N, and PO4-P concentration during the adsorption
50
Batch mode and continuous membrane capacitive deionization using flowing carbon
electrodes
Alexandra Rommerskirchen2, Youri Gendel1, Oana David1, Matthias Wessling1,2
1
DWI – Leibniz Institute for Interactive Materials, Aachen
2
RWTH -Aachen University, Aachener Verfahrentechnik-Chemical Process Engineering.
Continuous water desalination using Membrane Capacitive DeIonization (MCDI) process assisted with
flowing carbon electrodes is reported. Batch-mode experiments showed extremely high salt adsorption
capacities of 260 mg/g for the flowing activated carbon electrodes. A continuous process comprised of
desalinating and concentrating MCDI units and two recirculated flowing electrodes was operated at 50,
70 and 90% feed water (1gNaCl) split ratios. Desalination rates of more than 99% were achieved at > 90 %
water recovery, and were independent on the diluate/concentrate flow rate ratio.
Monday
15.30 - 16.50
Bentacera zaal
51
Hyper Salinity Desalination using Atlantis RDI Capacitive Deionization Technology
Patrick Curran
CEO, Atlantis Technologies, USA
Atlantis Technologies has developed the next generation capacitive deionization technology that enables
the practical desalination of industrial waste water exceeding 100,000 mg/l salinity. The technology was
developed in California for use on industrial waste waters such as oil/gas produced water, supersaturated
mining water, and flue gas desulfurization waters generated by coal fired power plants. This is possible
through dramatically increased flux rates, extended capacitors flow lengths, and unique system operation
which together increase the range of applications by a factor of 10 - 20. Our presentation will showcase
lab and field studies, flux rate characterizations, and system design.
Monday
15.30 - 16.50
Bentacera zaal
[email protected]; www.atlantis-water.com
52
Capacitive Deionization for Waste Water Re-use: Energy Efficiency Considerations
Cleis Santos1, Enrique García-Quismondo1, Jesús Palma1, Marc Anderson1,2
Electrochemical Processes Unit, IMDEA Energy Institute, E-28933, Mostoles (Madrid), Spain
1
2
Environmental Chemistry and Technology Program, University of Wisconsin-Madison, WI, USA 53706
(right). [4]
As result, in order to further optimize efficiency in the CDI process, particularly for 2 000 – 20 000 ppm
waste water concentration, we are systematically improving strategies for operating these systems in such
a way to achieve major impact on the practical application of this technology [4].
References
1. S. Porada, A. van der Wal, V. Presser, P.M. Biesheuvel, Review on the Science and Technology of Water Desalination by Capacitive
Deionization. Progress in Materials Science, 58 (2013) 1388-1442.
2. Avraham, E. Bouhadana, Y. Soffer, A. Aurbach, D. Limitation of charge efficiency in capacitive deionization. I. J. Electrochem. Soc.,
2009, 156 (6), 95-99.
3. P. Dlugolecki, A. van der Wal, Energy Recovery in Membrane Capacitive Deionization. Environ Sci Technol, 47 (2013) 4904-4910.
4. Garcia – Quismondo, E. Gómez, R. Vaquero, F. Cudero, A. L. Palma, J. Anderson, M. A. New testing procedures of a capacitive
deionization reactor. Phys. Chem. Chem. Phys., 2013, 15 (20), 7648-7656.
53
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Bentacera zaal
Figure 1 Charge-discharge configuration in decoupled procedures (left). Energy components in decoupled cycles
Monday
Due to the always increasing worldwide water scarcity associated to the climate change there is the need
to increase the reinjection of wastewater into the overall water cycle. The reuse of treated waste water
has been identified as a potential way for addressing long term imbalances between water demand and
water supply, therefore reducing the vulnerability of water and environmental resources to climate change and man-made pressures. This study provides a mechanistic analysis of Capacitive Deionization (CDI)
applied on Waste Water Re-use, paying special attention to Energy Efficiency aspects. CDI technology
is gaining increased scientific interest since 2006 [1]. However, not too many publications indicate the
feasibility of the kWh/m3 consumption in CDI systems. The common assumption proposes that the main
problem may be the ions adsorption capability of the electrode material during charging [2]. To our experience, desorption processes may be even more problematic, in energy efficiency terms, since they hold
diffusional difficulties when submitted to relatively high current densities [3].
This work provides an overview of current strategies for operating these systems aiming to improve energy
recovery and lead this process to the point of making these systems an option for use in waste water treatment plants. Experimental work includes consecutive deionization – regeneration tests conducted under
a combination of constant current and constant voltage steps at different current rates (close to real life
scenarios). A schematic representation of the performance profile proposed can be seen in Figure 1 (left)
[4].
Oral presentations Tuesday
Tuesday
55
Role of Surfaces in the Biochar Effect
Ellen R. Graber
Department of Soil Chemistry, Plant Nutrition and Microbiology
Institute of Soil, Water and Environmental Sciences
Agricultural Research Organization (ARO)
The Volcani Center, Bet Dagan 50250, Israel
Tel: 972-3-968-3307; Fax: 972-3-960-4017
email: [email protected]
Tuesday
9.50 - 11.10
Rabobank zaal
Home page: http://www.agri.gov.il/en/people/680.aspx
Intensive research in the last decade into agronomic impacts of soil amendment with biochar, the solid
co-product of biomass pyrolysis, has revealed that many soil chemical and biological characteristics may
be altered when biochar is added to soil: pH, Eh, microbial diversity and community structure, greenhouse
gas emissions, nutrient retention, soil physical structure, water retention, and more. These changes can
affect plant growth, productivity, and resistance to stress when grown in biochar-amended media. A major
challenge today is to understand which biochar characteristics are responsible for this “Biochar Effect”.
Biochar surfaces are highly heterogeneous and reactive, and interactions occurring at or being promoted
by those surfaces may play a role in many of the observed effects. For example, biochar surfaces have a
relatively high content of pH-dependent cation exchange sites [1], and this content increases as biochar
ages in the soil. This means that biochar absorbs cationic nutrients such as NH4+, and also releases them
for plant utilization; retention capacity for cations increases as biochar ages in the soil. In contrast, biochar
has virtually no anion exchange capacity, meaning that nutrients such as NO3- and PO4- are not retained as
anions. Reduction reactions promoted by biochar surfaces and biochar-borne phenolic compounds and
humic-like substances can cause dissolution of soil Fe and Mn oxides, releasing these nutrients into solution [2]. Biochar-derived, water soluble humic-like substances can complex with these released elements
much as do humic and fulvic substances, increasing their plant availability. Redox active biochar surfaces and molecules can promote microbial activity by acting as electron shuttles. Biochar surfaces adsorb
pathogenic enzymes and toxins, helping to protect plants, and the adsorbent surfaces can interact with
plant root exudates changing the profile of those exudates in the soil and hence the microbial community
structure [3]. These and many other attributes of biochar surfaces can make important contributions to
biochar effects in the soil.
References
1. Silber, A., Levkovitch, I., Graber, E. R. (2010) Environ. Sci. Technol. 44: 9318-9323.
2. Graber, E.R., Tsechansky, L., Lew, B., Cohen, E. (2014). Eur. J. Soil Science, 65: 162-172.
3. Graber, E.R., Frenkel, O., Jaiswal, A.K., Elad Y. (2014) Carbon Management, 5: in press.
56
Phosphate adsorption on hydrous ferric oxide and its effect on the re-growth of broken
flocs
Wenzheng Yua and John Gregoryb
a
Department of Civil and Environmental Engineering, Imperial College London, London SW7 2AZ, UK
([email protected])
b
Department of Civil, Environmental and Geomatic Engineering, University College London, Gower Street, London WC1E 6BT, UK.
([email protected])
Phosphate adsorption on hydrous oxide flocs is important for aquatic environmental processes and in the
treatment of water with hydrolyzing coagulants. Removal of phosphate from surface waters can be achieved either by adsorption on suitable adsorbents or by chemical precipitation. Under most practical conditions, hydrolyzing coagulants, such as salts of aluminium or iron(III) produce an amorphous precipitate of
the hydrous oxide which can be very effective in the removal of both particulate and soluble impurities,
the latter including dissolved organic material and phosphates.
57
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Adsorbed phosphate has a major influence on the growth of flocs. Depending on pH and phosphate concentration, floc growth may be either enhanced or imhibited. Breakage of HFO flocs by high shear is
known to be irreversible to some extent, so that broken flocs do not re-grow completely after the shear is
reduced. It has been found that addition of phosphate during floc breakage can entirely prevent re-growth
and this is closely related to phosphate adsorption. By considering the nature of surface groups on HFO
and the nature of bonding within HFO flocs a model for the breakage and re-formation of flocs is proposed, which can explain the irreversible nature of floc breakage. The role of phosphate in this process will
also be considered.
Tuesday
In the present work a systematic study has been carried out of the interaction of orthophosphate with
hydrous ferric oxide (HFO) precipitate, at different pH values and with fresh and aged precipitate. HFO is
initially precipitated as very small particles a few nm in size, which can then aggregate to form much larger
flocs (up to several hundred µm). In the absence of phosphate, stirring of flocs at high shear causes some
reduction in pH, which is most significant in the pH range 8-10. As has been previously found, phosphate
adsorption decreases with increasing pH and is significantly lower after aging of the precipitate. At pH
values greater than 5, phosphate adsorption on HFO causes an increase in pH, indicating binding of H+ or
release of OH-. By a pH-controlled titration procedure, the change in OH- concentration could be determined for a range of phosphate additions. These were compared with the amounts of phosphate adsorbed
under the same conditions. The results showed significant effects of both pH and precipitate age.
Effect of phosphate sorption on Ferralsol dispersion: Evaluation with stability ratio and
repulsive potential energy
Dung Viet Pham1,A, Munehide Ishiguro1, Ha Thu Thi Tran2
Hokkaido University, Japan, 2Hue University of Agriculture and Forestry, Vietnam
1
Email: [email protected]
Soil dispersion induces soil erosion and colloidal leaching. The phosphate (P) sorption results in increase
of net negative charge. The influence of phosphate on soil dispersion must be evaluated well in order to
control soil erosion and leaching. In this study, influence of P sorption on Ferralsol soil dispersion was
investigated by calculating repulsive potential energy based on zeta potential and stability ratio of soil
suspension. Ferralsol which is a typical soil in rainy tropical region was used as the material. We have
used monovalent (Na) and divalent (Ca) ions in 1mmolc L-1 equilibrium salt solution. The batch method of
phosphate sorption experiments was conducted at different pH 4, 5.5, 7 and 8.5 by adding NaH2PO4 or
Ca(H2PO4)2. Salt concentration was supplemented by NaNO3 or Ca(NO3)2 when the adding phosphate concentration was less than 1 mmolc L-1. Salt concentration increased when > 1mmol L-1P was added in some
cases. Stability ratio (W), derived from dynamic light scattering method, was used to evaluate stability of
colloid suspension. Stability ratio was calculated by kf/k; kf is the rate of fast coagulation and k is the coagulation rate of the sample under consideration. The repulsive potential energy between the soil colloids
when they approach at 1 nm was calculated using the zeta potential and the diffuse double layer theory.
Generally, the stability ratio increased with increasing pH because the negative charge of the soil increased
with increasing pH. In Na system, the stability ratio increased when P sorption increased up to around 10
mmol P kg-1. When P was sorbed, the soil charge became more negative and the soil dispersed well due
to the electric repulsive force. After the peak, it decreased with increasing P sorption at > 10 mmol P kg-1
because of the increase of electrolyte concentration (>10 mmolc L-1 Na). In Ca system, similar trend was
observed. However, the stability ratio increased again at around 250 mmol P kg-1 at pH 7 & 8.5 probably
because of the decrease of electrolyte concentration after Ca-P precipitation. Stability ratio increased with
the increase of repulsive potential energy (Fig. 1). The stability of the soil was evaluated with the repulsive
potential energy. In Na system, the soil flocculated well when the repulsive potential energy was < 0.1
μJ m-2, corresponding with logW <1.15. Soil dispersed well when logW >1.4 at repulsive potential energy
>0.19 μJ m-2. In Ca system, at the energy <0.06 μJ m-2 the soil flocculated well (logW<0.17). At the energy
>0.36 μJ m-2 the soil dispersed well (logW>1.14).
2
Stability ratio (LogW)
Tuesday
9.50 - 11.10
Rabobank zaal
A
1,5
1
0,5
0
0,01
0,1
1
2 10
Repulsive potential energy (μJ/m )
Fig. 1 Repulsive potential energy and stability ratio
◇pH 4, □pH 5.5, △pH 7, ○pH 8.5 for Ca(NO3)2 concentration
◆pH 4, ■pH 5.5, ▲pH 7, ●pH 8.5 for Na(NO3)2 concentration
........... electrolyte concentration ≤ 1 mmolc L-1
- - - - - 1 mmolc L-1< electrolyte concentration ≤ 10 mmolc L-1
_____ electrolyte concentration >10 mmolc L-1
58
Plasma Polymer Coated Particles: A New Class of Adsorbents for Water Purification
Behnam Akhavan*, Karyn Jarvis, Peter Majewski
University of South Australia, School of Engineering, Mawson Institute, Adelaide, SA 5095, Australia
* E-mail: [email protected], Website: http://people.unisa.edu.au/Behnam.Akhavan
Tuesday
In recent years, functionalized hydrophobic materials have attracted considerable interest as petroleum
hydrocarbon removal agents. This investigation has applied plasma polymerization as a novel, green and
one-stage process [1] to develop nanostructured hydrophobic and oleophilic films for water purification.
1,7-Octadiene was plasma polymerized onto silica particles using a radio frequency inductively coupled
reactor fitted with a rotating chamber. Plasma polymerized 1,7-octadiene (ppOD) films were deposited
using a varied range of plasma power, 1,7-Octadiene flow rate and deposition time. The surface chemistry of ppOD coated particles was investigated via X-ray photoelectron spectroscopy and time-of-flight
secondary ion mass spectroscopy, while Washburn capillary rise measurements were applied to evaluate
the hydrophobicity and oleophilicity of the particles. The effectiveness of ppOD coated particles for the
removal of hydrophobic matter from water was demonstrated by adsorption of motor oil, kerosene, and
crude oil. Petroleum hydrocarbon removal was examined by varying removal time and particle mass. The
morphology of oil loaded ppOD coated particles was examined via environmental scanning electron microscopy observations. Increasing the polymerization time increased the concentration of hydrocarbon
functionalities on the surface (Fig. 1), thus also increasing the hydrophobicity and oil removal efficiency
(ORE) [2,3]. The ppOD coated particles have shown to have excellent ORE. These particles were capable of
removing 99.0−99.5% of high viscosity motor oil in 10 min, while more than 99.5% of low viscosity crude
oil and kerosene was adsorbed in less than 30s. Plasma polymerization has shown to be a promising approach to produce a new class of materials for a fast, facile, and efficient oil removal.
9.50 - 11.10
Rabobank zaal
Fig. 1. ToF-SIMS CH- ion maps for uncoated and coated particles for different times
References1
1. Akhavan, B.; Jarvis, K.; Majewski, P., Hydrophobic plasma polymer coated silica particles for petroleum hydrocarbon removal.
ACS Appl. Mater. Interfaces 2013, 5, 8563-71.
2. Akhavan, B.; Jarvis, K.; Majewski, P., Tuning the hydrophobicity of plasma polymer coated silica particles. Powder Technol. 2013,
249, 403-411.
3. Akhavan, B.; Jarvis, K.; Majewski, P., Evolution of Hydrophobicity in Plasma Polymerised 1,7-Octadiene Films. 2013, 10, 10181029.
59
Keynote
Characterization of droplets produced by
electrospray emulsification
Anne Kamau1, Jan C.M. Marijnissen2, Luewton L.F. Agostinho1,3
1 Wetsus Centre of excellence for sustainable water technology,
Oostergoweg 7, 8911 MA Leeuwarden, The Netherlands
2 Aerosol Consultancy, Zaart 11, 4819 ED Breda, the Netherlands
3 NHL, University of Applied Sciences, Rengerslaan 10, P.O. Box 1080,
Tuesday
9.50 - 11.10
Nivo Noord zalen
8900 CB Leeuwarden, the Netherlands
Electrohydrodynamic atomization (EHDA) provides a novel way to enhance the dispersion of droplets in a
liquid media, therefore to create highly homogeneous (droplet size) emulsions. emulsion and improve its
quality. The effectiveness of this technique is already proven by some authors (see reference list) and was
further investigate in this work regarding its capability to produce micro size, well dispersed and highly
charged droplets emulsions. Various liquid-liquid combinations were selected. The liquid combinations
were initially tested to identify which could produce a stable cone-jet mode, i.e. small size droplets with
narrow distribution. After selecting the most appropriated liquid combinations, the produced emulsions
were further characterized in terms of the droplet diameter and size distribution, the emulsion quality,
electrical energy requirements. Additional studies were performed to study the suitability of applying theoretical scaling laws to predict the droplet size and spray current. One of the selected liquid combinations,
e.g. ethylene glycol-hexane, was found to generate stable cone-jet mode between 6 and 8 kV for a range of
flow rate of 0.5- 4.0 mL/h. In this mode, the measured average droplet diameter was found to range from
2- 14μm and a bimodal size distribution was observed. The droplet dispersion into the continuous phase
was enhanced by the electric field and by self-repulsion. The stability of the droplets in the continuous
phase was found to increase in the presence of a surfactant (Tween 80). Preliminary results showed that
the electric energy requirements were in the scale of 106J/m3. The average droplet diameter was found
to scale with the liquid flow rate as in d~Q0.33 and the dimensionless current scaled with the flow rate by
I/I0~ (Q/Q0)0.5. The study has, therefore, indicated that EHDA can be effectively used in the preparation
of emulsions.
References
1. Barnes and I. Gentle, Interfacial Science - An introduction. Oxford University Press. 2005
2. Mc Clements, Critical review of techniques and methodologies for characterization of emulsion stability. Critical Reviews in Food
Science and Nutrition. 2007. 47(7): p 611-649
3. J. F. Hughes and I. D. Pavey, Electrostatic emulsification. Journal of electrostatics.1981.10: p 45-55
4. Geerse, Applications of electrospray: From people to plants. PhD Theis.2003
60
Simultaneous production of high quality water and electrical power from aqueous
feedstocks and waste heat by high pressure membrane distillation
Norbert J.M. Kuipers, Jan Henk Hanemaaijer, Hans Brouwer, Albert Jansen (TNO)
Frank W. Altena and Peter van der Vleuten (Free Energy & Water), Henk Bak (E.ON)
TNO, Water Treatment Department (Utrechtseweg 48, 3704 HE Zeist, The Netherlands)
T +31 (0)88 866 21 67, [email protected])
A new membrane distillation concept (MemPower) has been developed for the simultaneous production
of high quality water from various aqueous feedstocks with cogeneration of mechanical power (electricity). Driven by low grade waste heat a pressurized distillate can be produced by operating TNO’s Memstill®-process at high hydraulic pressures. These pressures are theoretically limited by the Liquid Entry
Pressure (LEP) of the membrane. The proof of principle has been shown and is based on the transport of
water vapor against a hydraulic pressure gradient. Various existing and new types of membranes have
been evaluated in order to obtain high yields in water flux and power densities. Power densities have
been measured which are sufficient to drive the pumps in membrane distillation. This allows standalone
Memstill-units without electricity consumption to be possible, which are fully driven by waste heat. The
application of new incompressible hydrophobic membranes, combining a high permeance with a high LEP,
will allow for much higher power densities.
Tuesday
9.50 - 11.10
Nivo Noord zalen
61
Investigating the fouling stages during membrane filtration of silica nanoparticle
solutions
Krzysztof Trzaskus1, *, Antoine Kemperman1, Kitty Nijmeijer1
Membrane Science & Technology, MESA+ Institute of Nanotechnology, University of Twente, Faculty of Science and Technology, 7500
AE, Enschede, The Netherlands.
Tuesday
9.50 - 11.10
Nivo Noord zalen
* [email protected]
In the last decade many new nanotechnology based products have been developed. This causes a worldwide exponential growth in the production volume of nanoparticles (NPs). The impact of manufactured
NPs on living organisms is still under discussion. However, most researchers suggest that NPs are toxic. It
is obvious that after usage the manufactured NPs will accumulate in the aqueous environment. Therefore,
sustainable growth of nanotechnology requires an environmentally-friendly technology to remove NPs
from potential drinking water sources. A promising technique to remove nano-sized contaminants from
water is based on membranes. However, not much is known on the filtration and fouling behavior of NPs
in membrane processes.
Ultrafiltration and especially microfiltration membranes are prone to internal fouling and pore blockage
caused by the presence of NPs having a diameter smaller than the pore size of the membrane applied.
The small size of NPs results in a high surface area to volume ratio, which significantly enhances the role of
surface interactions on the stability of the NP suspensions. On the other hand, the stability of NP suspensions and in fact their tendency to aggregation strongly affect the fouling mechanism during membrane
filtration of the NPs.
In this experimental study, fouling and rejection of mono-dispersed model NPs were investigated. A microfiltration hollow fiber membrane was employed in dead-end filtration mode for the filtration of commercially available silica nanoparticles under constant pressure. Applying a low concentration of NPs and
a large difference between the membrane (~200 nm) and the nominal size of the NPs (22 or 7 nm) allowed
detailed investigation of the fouling mechanisms. Base on filtration and rejection data, four fouling stages
were proposed: adsorption, electrostatic blockage effect, pore blocking, and cake filtration. The occurrence and character of these stages were strongly affected by the ratio between particle size and pore size.
Furthermore, it was found that solution properties like the presence of salts, the pH or the valency of the
cation strongly alter fouling and rejection behavior. The observed effects of the solution properties was
explained using the DLVO theory, which describes colloidal stability and the role of solution properties.
Lower repulsive interactions between the nanoparticles accelerate fouling by faster pore blockage and
aggregation on the membrane surface. The rejection of the NPs was improved by instantaneous pore
clogging and formation of a deposit on the top of the membrane surface. Porosity of the filtration cake
layer on the membrane surface was strongly dependent on the NPs solution properties. This paper clearly
shows that the filtration of NPs can be optimized by choosing the right practical conditions.
62
Transport of Sewage-borne Ammonium in a Floodplain Aquifer: Column Experiments
with Aquifer Materials from the Yamuna Floodplain in Delhi (India)
Maike Groeschke1, Theresa Frommen2, Gesche Grützmacher3, Michael Schneider2
1 Freie Universität Berlin/ Kompetenzzentrum Wasser Berlin, Germany
2 Freie Universität Berlin
3 Kompetenzzentrum Wasser Berlin
[email protected], www.geo.fu-berlin.de/hydrogeology, www.kompetenz-wasser.de
1. Repert, D. A., Barber, L. B., Hess, K. M., Keefe, S. H., Kent, D. B., Leblanc, D. R. and Smith, R. L. (2006) Long Term Natural Attenuation of Carbon and Nitrogen within a Groundwater Plume after Removal of the Treated Wastewater Source. Environ. Sci.
Technology, 40, 1154-1162.
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References
Tuesday
The Yamuna River is the biggest tributary of the Ganga River in the Indo-Gangetic plain and it flows through
the mega city Delhi in North-South direction. Owing to a fast growing population, the river stretch in Delhi
is highly influenced by untreated or partially treated sewage water. Dissolved oxygen concentrations in the
river are often below 1.0 mg/L during the winter months and the prevailing form of nitrogen is ammonium, which was measured in concentrations of up to 20 mg/L in 2012/13. In recent years, elevated ammonium concentrations were observed at a riverbank filtration site in central Delhi, which was constructed
in 1973. Here ammonium concentrations of up to 30 mg/L were measured in hand pumps at a distance of
250 m to the riverbank and concentrations between 5 and 8 mg/L were found in a large horizontal collector well (Ranney well) at a distance of 500 m to the river during normal well operation.
Due to cation exchange reactions, ammonium is generally retarded in the groundwater flow. Transformation or degradation of ammonium can occur along the flow path as nitrogen is a redox sensitive species and
ammonium oxidation can take place (either anoxic – anammox, or oxic – nitrification). Furthermore, the
permanent fixation of ammonium in the sediment can also remove ammonium from the system. Mineralization of organic nitrogen can be an additional source of ammonium (Repert et al. 2006). These processes
are all strongly related to the sediment characteristics and thus a quantitative prediction of future ammonium concentrations is not possible without knowing the site-specific ammonium-sediment interactions.
Column experiments were conducted with artificial oxic and anoxic groundwaters and aquifer material
from different representative zones of the aquifer, which has a thickness of 17 m and consists of a bottom
gravel layer and overlying medium grained sands which tend to be more fine-grained towards the top.
Results show that sediments from a distance of 35 m and 250 m from the riverbank are in equilibrium
with the groundwater, whereas disequilibrium between adsorbed ammonium on the exchanger and ammonium in the groundwater can be observed at 500 m distance, indicating that this is the current front
of the ammonium plume. In the adsorption and desorption experiments, the predominant process observed in the deeper sediments from depths > 25 ft (gravel and sand) was cation-exchange (sorption and
desorption), with gravel showing slower reaction kinetics than the sand (30 vs. 15 flushed pore volumes
to release all adsorbed ammonium). This was unexpected and the reason for the retardation is still under
investigation. Only in the very top layer of the aquifer at a depth of 3 m degradation or fixation of 30-55%
of the ammonium input was detected.
The results of the column experiments will be used to set up a 1D reactive transport model for the transport of ammonium at the field site in order to model future water quality scenarios. This is necessary to
evaluate the suitability for future drinking water production and to plan appropriate treatment options.
Ion adsorption at mineral-electrolyte interfaces probed by high resolution Atomic
Force Microscopy
Prof. Dr. Frieder Mugele
Univ. Twente – MESA+ Institute for Nanotechnology – Physics of Complex Fluids
The distribution of ions and charge at solid-water interfaces plays an essential role in a wide range of
processes in biology, geology and technology. While theoretical models of the solid-electrolyte interface
date back to the early 20th century, a detailed picture of the structure of the electric double layer has
remained elusive, largely because of experimental techniques have not allowed direct observation of the
behaviour of ions, i.e. with subnanometer resolution. We have made use of recent advances in Atomic
Force Microscopy (AFM) to reveal, with atomic level precision, the ordered adsorption of the mono- and
divalent ions that are common in natural environments to heterogeneous gibbsite/silica surfaces in contact with aqueous electrolytes. Complemented by density functional theory, our experiments produce a
detailed picture of the formation of surface phases by templated adsorption of cations, anions and water,
stabilized by hydrogen bonding. In particular, we demonstrate the sequential build-up of the Stern layer by
consecutive adsorption of Ca2+ and Cl- ions upon increasing the bulk concentration of CaCl2. Simultaneous
measurements of the charge in the diffuse layer using AFM spectroscopy suggest that deprotonation of
hydration water largely compensates the charge due to cation adsorption.
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7500AE Enschede (The Netherlands)
64
Pore-scale study of processes and transport in porous media; an overview
T. Sweijen, S.M. Hassanizadeh, N. K. Karadimitriou, Q. Zhang
Utrecht University; Department of Earth Sciences, The Netherlands
Website: http://www.geo.uu.nl/~wwwhydro/
To increase our insight of flow and transport phenomena in porous media on both micro- and macro
scales, pore-scale studies are essential. Studies have included chemical, biological, and physical applications. Experimentally, micro-models have been proven to be a valuable tool as they allow the observation
of flow and transport phenomena on the micro-scale. A micro-model is an artificial representation of a
porous media, made of a transparent material. We have used Poly-Di-Methyl-Siloxane (PDMS), which is a
viscoelastic, silicon-based organic polymer. It is optically transparent, inert, non-toxic, and non-flammable.
We have performed two-phase flow and colloid transport experiments in these micro-models. We have
established that the inclusion of fluid-fluid interfacial area allows for the modelling of the hysteretic relationship between capillary pressure and saturation in porous media. In other words, data points of capillary
pressure-saturation-interfacial area from many (scanning) drainage and imbibition experiments fall on a
single surface. In colloid transport experiments, we directly observe colloids movement, their retention at
interfaces between phases, and their mobilization by moving interfaces and contact lines.
Another valuable tool is pore-scale modeling, which allows us to conduct numerical “experiments”, from
which closure equations for macro-scale description can be obtained. Currently, we are using a Discrete
Element Method to study the coupling between swelling porous media and pore fluid flow.
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65
The Dynamics of Micro-vortices During Overlimiting Electrodialysis
J. C. De Valença1,2, R. M. Wagterveld1, R. G.H. Lammertink2 and P. A. Tsai2
Wetsus, centre of excellence for sustainable water technology, Oostergoweg 7, 8911 MA Leeuwarden, The Netherlands. 2Soft Matter,
1
Fluidics and Interfaces, MESA+ Institute of Nanotechnology, University of Twente, P.O. Box 217, 7500 AE Enschede, The Netherlands.
We experimentally investigate the coupled dynamics of global ion-flux and local hydrodynamics of an
electrolyte solution close to a charge selective membrane under an electric forcing. At small voltages, cations transport diffusively across a cation exchange membrane (CEM), whereas the transport of oppositely
charged anions is blocked, causing the main resistance of the system. At higher voltages this resistance
suddenly increases and in addition to diffusive transport, hydrodynamic convection sets in within a boundary layer of O(100 µm), resulting in the so-called over-limiting current. In this regime we measured the
fluid flow with particle image velocimetry (PIV) combined with chronopotentiometric resistance measurements for the first time. Our results reveal that the micro-vortices are caused by gravitational unstable
gradients and by electro osmotic-coupling between the membrane surface and the solution. Moreover,
under a constant applied electric current, the electroconvective micro-vortices start with a voltage jump
and grow linearly both in size and speed. After this initial linear growth, the resultant voltage levels off
around a fixed value. The average vortex size stabilizes as well, however the individual vortices are unsteady and dynamical. Our experimental setup and results offer a complete picture of the coupled dynamics
of the hydrodynamics and electrical responses of an electrolyte, beneficial for characterizing a variety of
charge selective membranes in order to improve electrodialysis desalination processes.
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Website: http://www.utwente.nl/tnw/sfi/people/PhD%20Students/Valenca/
66
Water Purification and Brine Concentration by Shock Electrodialysis
Sven Schlumpberger1, Matthew Suss1, Daosheng Deng1,2, Ali Mani1,3, Martin Z. Bazant1,4
Department of Chemical Engineering, MIT 2School of Engineering and Applied Sciences, Harvard 3Department of Mechanical Engi-
1
neering, Stanford 4Department of Mathematics, MIT, USA
Email: [email protected]
Website: http://web.mit.edu/bazant/www/group/
Tuesday
In this project, we investigate experimentally and theoretically the possibility of exploiting deionization
shocks in porous media for water purification and brine concentration by “shock electrodialysis”. The basic idea of this new approach is to drive an over-limiting current (faster than diffusion) through a charged
porous medium sandwiched between two cation-exchange membranes, perpendicular to a pressure-driven cross flow, which produces a sharp “shock” in the salt concentration profile between deionized and
concentrated steams, which are separated at the outlet. In contrast to classical electrodialysis, only one
membrane type is needed to trigger the phenomenon, and the separation is effectively “membraneless”
within the porous medium. Boundary layer analysis, generalizing the Leveque solution for over-limiting
current, provides useful engineering principles, and detailed simulations of the system help us gain insight
into the phenomena at play. We demonstrate the principles of shock ED experimentally in a sequence of
prototypes. Initially we use copper electrodes and copper sulfate solution to demonstrate the feasibility of
the project and then replace the copper electrodes with electrode streams sustaining the current by water
electrolysis, as in traditional ED, in order to be able to use this phenomenon to remove a wide range of
electrolytes, including sodium chloride, from water. The results show reasonable efficiency and unique separation capabilities, such as removal of particles and disinfection, that may find applications in compact
water treatment and brine concentration.
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67
Dynamic adsorption of pharmaceutical residues at trace concentrations onto activated
carbon cloths
Hélène FALLOU, Nicolas CIMETIERE, Sylvain GIRAUDET, Dominique WOLBERT, Pierre LE CLOIREC
Ecole Nationale Supérieure de Chimie de Rennes, CNRS, UMR 6226, 11 allée de Beaulieu, CS 50837, 35708 Rennes Cedex 7, France
Université Européenne de Bretagne
Contact : H. Fallou, Tel 02-23-23-80-83
mail : [email protected]
Several studies have shown the occurrence of pharmaceutical residues into various aquatic compartments
. This pollution is not totally removed by the usual treatments. Some compounds like diclofenac or carbamazepine are thus found in drinking waters. Adsorption processes (using activated carbons) are promising to remove these undesirable compounds from raw waters. Furthermore, activated carbon fiber cloths
(ACFC) have shown many advantages for water treatment [3] since these adsorbents possess high specific
surface areas, and more particularly, narrow pore size distributions, which enhance their affinity and selectivity towards these pollutants at trace concentrations.
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[1-2]
The first part of our study dealt with the determination of adsorption kinetics and isotherms for four
different chemical species (acetaminophen, caffeine, diclofenac and carbamazepin). These experiments
were carried out using batch reactors but with environmental conditions (i.e. initial concentrations of
1 µg/L and in the presence of natural organic matter). Therefore, maximum adsorption capacities were
determined as well as an efficient isotherm models (Langmuir-Freundlich). The competition with other organic molecules was especially critical when dealing with trace concentrations of the targeted compound.
If the natural organic matter have a low impact on adsorption capacities at high concentrations, the impact
is very important at the lowest aqueous concentration (up to - 60 % of the single-component adsorption
capacity). Parting addition, the competition with the organic matter involved a large decrease of the adsorption rate. More precisely, the most impacted coefficient for mass transfer is the surface diffusivity
(from the application of the homogeneous surface diffusion model).
Following this first approach (in batch conditions), the second part of the study focused on the dynamic
adsorption of the four compounds. Breakthrough curves were determined using an experimental unit
that was designed for a maximum flow rate of 100 L/h and inlet concentrations of the pharmaceutical
residues of 1 µg/L. Various operating conditions were tested and their influence was evaluated: the type
of water (tap water, surface water with different contents of natural organic matter), the velocity of the
liquid through the filter, the thickness of the filter (i.e. the number of layers of ACFC), and the type of ACFC.
The adsorption in dynamic conditions was then compared with the characteristics obtained in the batch
experiments (mass transfer coefficients, adsorption capacities, influence of the competitions).
68
Adsorption of chitosan from aqueous solutions onto silica
Alberto Tiraferri, Diana Caro Rodriguez, Plinio Maroni, Michal Borkovec
Department of Inorganic and Analytical Chemistry, University of Geneva, Sciences II, Quai Ernest-Ansermet 30, 1205 Geneva, Switzerland
[email protected], http://colloid.ch/
Chitosan is the only cationic polymer originated from natural sources and is widely employed as a biomaterial for numerous systems and in the most diverse fields. Few studies address the fundamental question
of the adsorption mechanism of chitosan on negatively charged surfaces. However, an understanding of
this adsorption behavior is important to the rational design and to the advancement of the environmental
and engineering systems applying chitosan as a functional material.
pH 8
pH 9
Low Salt
High Salt
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pH 4
Tuesday
We present the adsorption behavior of chitosan onto silica from aqueous solution. The adsorption behavior and the resulting layer properties are investigated by combining optical reflectometry and the quartz crystal microbalance. The same surfaces are used to measure the amount of
adsorbed chitosan with both techniques, allowing the systematic combination of the respective
experimental results. Therefore, we determine layer thicknesses and their water content for
chitosan adsorbed on silica from aqueous solutions of varying composition. In particular, we
study the effect of pH at 10 mM NaCl and we focus on the influence of electrolyte type and concentration for two representative pH conditions.
In mildly acidic solutions, chitosan behaves like a weakly charged polyelectrolyte, whereby electrostatic attraction is the main driving force for adsorption. Under these conditions, chitosan
forms rigid and thin adsorption monolayers with an average thickness of approximately 0.5 nm
and a water content of roughly 60%. The tendency of chitosan to form highly swollen and relatively large aggregates is confirmed in neutral solutions, whereby adsorption layers become
significantly thicker (~10 nm) as well as soft and dissipative. These films are also characterized
by a highly hydrated state containing up to 95% of water.
This study demonstrates that chitosan forms stable adsorption layers on oppositely charged silica surfaces under a wide range of chemical conditions. Significantly different films can be obtained by fine tuning the adsorption conditions. In particular, the possibility to produce tailored
adsorption layers simply by adjusting the solution pH represents a remarkable opportunity to
use this polyelectrolyte in a variety of systems targeted for different purposes.
Sacrificial polymer layers for easy membrane cleaning
Shazia Ilyas*, Wiebe M. de Vos and Kitty Nijmeijer
Membrane Science and Technology, University of Twente, P.O. Box 217, 7500 AE
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Enschede, The Netherlands. E-mail: [email protected]; Tel: +31 53 489 3474
Fouling constitutes a major problem in membrane technology and leads to a reduced production capacity
and increased operation cost. This research presents a solution for membrane fouling based on a polymeric “Sacrificial Layer” approach. One of the options available to control fouling is surface modification of
the membranes. To modify and tune the surface of an ultrafiltration membrane with desired properties
the most promising method seems to be the layer-by-layer (LbL) electrostatic self-assembly leading to
polyelectrolyte multilayer (PEMs) formation [1]. PEM are coated using LbL approach involving alternating
sequential adsorption of polycations and polyanions onto a charged surface. The number of deposited
layers determines the thickness of a PEM membrane (PEMM) and thus selectivity and flux can be tuned
by the number of LbL cycles or by the chemical composition of the utilized polyelectrolytes (PEs) [2]. Now
the PEM layers of a few nanometers thickness can also be removed by simple trigger such as a change
in pH or salt concentration. This so-called “sacrificial layer” approach, allows the possibility that when
fouling agents get adsorbed on the surface of the membrane, they can be removed by simply desorbing
(sacrificing) the polymer coating in solution. An extra benefit might be that the polyelectrolytes that are
released into solution upon destruction of the layer could well act as so-called anti-redeposition agents: by
adsorbing to the released fouling agents they could prevent possible re-adsorption of the fouling agents.
This concept is schematically shown in Fig. 1. To give a “proof of principle” for the application of such multilayers as sacrificial layers for membrane technology we use polyelectrolyte multilayers in combination
with model foulants such as silica particles and BSA (bovine serum albumin). Such proof of principle of
the sacrificial layer approach has been provided for a silicon substrate [3] but not yet for applied systems
such as membranes. We investigate the growth of a new LbL system including the interaction with model
fouling agent via reflectometry. Then to sacrifice these layers, including the fouling agent, the effect of
appropriate trigger (based on low pH and a high salt concentration) will be discussed. We demonstrate the
effectiveness of the approach both on model surfaces and on a hollow fiber ultrafiltration membrane. To
check the efficiency of the modified membrane, permeability and retention results will be discussed along
with the effect of trigger
Fig. 1. Schematic representation of polyelectrolyte multilayer as a sacrificial layer. Fouling agents are adsorbed to the
multilayer but upon a change of the pH, the layer desorbs, taking with it the adsorbed fouling particles. Released polyelectrolytes cover the particles and prevent re-adsorption.
References
1. Magnenet, C., Jurin, F. E., Lakard, S., Buron, C. C., & Lakard, B. (2013). Polyelectrolyte modification of ultrafiltration membrane
for removal of copper ions. Colloids and Surfaces A: Physicochemical and Engineering Aspects, 435, 170-177. doi: 10.1016/j.
colsurfa.2012.12.028
2. Joseph, N., Ahmadiannamini, P., Hoogenboom, R., & Vankelecom, I. F. J. (2014). Layer-by-layer preparation of polyelectrolyte
multilayer membranes for separation. Polymer Chemistry. doi: 10.1039/c3py01262j
3. [3] de Vos, W. M., de Keizer, A., Stuart, M. A. C., & Kleijn, J. M. (2010). Thin polymer films as sacrificial layers for easier cleaning.
Colloids and Surfaces A: Physicochemical and Engineering Aspects, 358(1–3), 6-12. doi: http://dx.doi.org/10.1016/j.colsurfa.2009.12.022
70
Colloidal flocculation of PSL particle induced by an adsorption of polyelectrolyte
studied in relatively concentrated suspension
Y.Adachi, T.Takanashi, S.Adaka, M.Kobyashi
Graduate School of Life and Environmental Sciences, University of Tsukuba, Japan
[email protected]
Flocculation of polystyrene latex (PSL) particles induced with oppositely charged polyelectrolytes are investigated near the regime of optimum flocculation concentration (OFC) as a function of ionic strength and
colloid concentration. Flocculation is performed by mixing of 5 ml colloidal dispersion with same amount
of polyelectrolyte solution by end-over-end. Results were evaluated by eventual sediment, electrophoresis and microscopic observation of floc morphology. The sedimentation test revealed that separation
by flocculation is practically induced only in the limited range of polyelectrolyte dosage around OFC over
which the colloidal dispersion is stabilized by the effect of reversed charge due to absorbed polyelectrolytes. It was confirmed that the condition of OFC corresponds to the condition where the charge of colloidal
particle is electrokinetically neutralized by the adsorption of oppositely charged polyelectrolyte irrespective of ionic strength and colloid concentration (Fig.1). Narrow and sharp window of separation around OFC
is observed under low ionic strength, while the width of separation window is broadened with an increase
of ionic strength. In the case of dilute suspension, the shift of i.e.p. with an increase of ionic strength was
observed implying the displacement of polyelectrolytes. The morphology of flocs formed in the former
is more or less rounded shape and compact structure, while under high ionic strength the morphology
showed up as elongated ellipsoid like rugby football.
Tuesday
PSL dispersion , N(0)=1.75×1010cm-3
○1.0×10-4M KCl △1.0×10-3M KCl □1.0×10-2M KCl
◇1.0×10-1M KCl
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Fig.1 Absorbance of supernatant (left) and electrophoretic mobility as a function of polyelectrolyte concentration for
Effects of MF membranes deformation and permeability on filtration of clay suspension
and its solution chemistry
Norazanita Shamsuddin and Diganta Bhusan Das
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Nivo Noord zalen
Department of Chemical Engineering, Loughborough University, LE11 3TU, UK
Emergency Events Database (EM-DAT) indicates global increase in the frequency and intensity of natural
disasters from 1900 to 2013. This is due to combinations of factors: climate change phenomena and population growth in vulnerable regions. One of first priorities after disaster is to provide safe drinking water
to the affected. Membrane technology offers several advantages over conventional treatment. It provides
better water quality, much more compact system, more flexible, less dependent on electricity and low
cost. Microfiltration (MF) membranes have been regarded as one of the oldest separation technique and
used extensively for the removal of particles, turbidity and microorganisms in water treatment. However,
membrane fouling and membrane deformation due to blocking and hydrostatic pressure respectively, are
limiting factors in water treatment. In understanding this issue, low pressure filtration of clay suspension
for water treatment purposes is investigated in this work. The effects of permeability due to variation in
solution chemistry of clay suspension, and deformation due to hydrostatic pressure are the parameters
studied. Clay is used as solid contaminant; one of multi-components of natural waters and hence, one
of the major factors that limits the use of MF for surface water treatment because it causes membrane
fouling. Clays are complex colloidal materials, thus their presence in water alter the performance of membranes due to their reactions with variations in solution chemistry as well as with water. Darcy’s law could
be used to explain apparent permeability change by changing the concentration of salt. This would explain
the electro-viscous effects by altering zeta potential and double layers measurement, and also membrane
resistance towards water. This study is important because membrane permeability control might prolong
the lifetime of the membrane for water treatment. Membrane deformation is investigated by measuring
pure water flux measurement prior to filtration experiment, and hysteresis phenomenon to be observed
whether reversible or irreversible membrane deformation has occurred.
72
MODIFIED HYDROPHOBIC CERAMIC MEMBRANES: USE FOR OZONE TRANSFER TO
WATER
A. Zouboulis1, S. Stylianou1 and M. Mitrakas2
Division of Chemical Technology, Department of Chemistry, Aristotle University of Thessaloniki, e-mail: [email protected].
1
Department of Chemical Engineering, Aristotle University of Thessaloniki , Greece
2
The financial support through the co- Financed by the European Union and the Greek State programme EPAN-II/ ESPA: ‘SYNERGASIA’
Project NanoMemWater, (09SYN-42-440) is gratefully appreciated. Thanks are due also to EKETA-Laboratory of Inorganic Materials
(V. Zaspalis, S.Sklari and A. Pagana) for the supplement of modified inorganic membranes.
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Acknowledgements
Tuesday
Membrane systems represent a relatively new and promising technology in the field of water/wastewater
treatment. However, membrane fouling and the relatively high energy demands prevent the wide scale
implementation of membrane processes. Chemical modification of membranes surface is a rather new
and innovate idea that has drawn the interest of many researchers. The key step of membrane modification is the introduction of active groups into the surface of membrane in order to improve their performance, for example by increasing hydrophobicity, and/or to satisfy different requirements (multi-functional
membranes).
In the present study, modified hydrophobic α-alumina membranes are evaluated for the transport of ozone to deionized water (mass transfer of ozone without reaction). Conventionally, ozone transfer to water
to be treated is mainly carried out via injectors, bubble columns or gas diffusers. Common feature of all
these techniques is the formation of bubbles; however, gas-liquid transport is a rate limiting process,
depending upon the ozone bubbles diameter. Such a process almost never results to a complete ozone
reaction, even when very small gas bubbles would be created; therefore, the ozone tank contactor suffers
from foam problems, while an ozone destructor is usually connected to the contractor for the removal of
non-reacted ozone gas. An alternative approach is the use of membrane contactors in order to optimize
the contact between the gaseous and aqueous phase. Previous studies have shown that the hydrophobic
membranes offer much higher efficiency of gas-liquid contact, than the hydrophilic ones. When water
comes in contact to a hydrophilic membrane it penetrates into the pores, due to the capillary forces. The
level of capillary pressure in hydrophilic porous media can be foreseen from theoretical approaches, as a
function of pore diameters and can reach quite high values, creating problems of gas transportation. On
the other hand, these problems can be overcome by the use of hydrophobic membranes. Mass transfer
coefficients for the examined ceramic membranes were calculated for different operating condition such
as pΗ, Reynolds number, temperature, etc.
A pneumatic micro-fluidic device for in-situ detection of mineral scaling at a membrane
surface
B. Liszka1, A.T.M. Lenferink1,H.S Rho3 G.-J. Witkamp2, C. Otto1
1
Department of Medical Cell BioPhysics, MIRA institute, University of Twente Enschede, The Netherlands; 2 Delft University of Tech-
nology Process & Energy Laboratory, Delft, The Netherlands; 3Department of Mesoscale Chemical System, MESA institute University
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of Twente Enschede, The Netherlands
Protecting surfaces against mineral scaling poses a great challenge in water processing technology. The
formed scale leads to a large decrease in membrane efficiency and large changes in surface properties
and, as a result, this leads simultaneously to increasing maintenance costs. Various methods to mechanically remove scale or slow down the process of scaling have been developed. Nevertheless, much can be
gained if very early stage scaling can be understood and prevented. For this reason, early scaling, under
in situ conditions needs to be investigated to enable a better protection of surfaces and facilitate water
quality control.
We propose here a pneumatic microfluidic device that is optically coupled with a Micro-Raman spectrometer as a method for in situ detection of sub-micron to nano-sized crystal formation on various organic
membranes.
The micro-fluidic system has been prepared using standard PDMS technology in combination with masks
made by photo-lithography. In order to create small, separate chambers on a chip, in which pre-nucleation
and mineralization takes place, the PDMS walls are pneumatically closed. The advantage of this pneumatic micro fluidic device is that it enables control over mass transport such that experiments can be carried out in a confined volume and under well-defined conditions in solution. Additionally, Raman-based
micro-spectroscopic methods like spontaneous Raman scattering and coherent Raman imaging can be
applied on samples under ambient conditions in the micro-fluidic device in real time. Another aim of this
work is to show that micro-fluidic devices are promising tools for studies concerning mineralization processes and will help to provide more information on underlying principles. The Raman spectra of minerals
are directly informative with respect to the chemical composition and can be directly interpreted in terms
of the symmetry of the crystals in case of different polymorphs. Furthermore, a great advantage is the
sensitivity which is sufficient to detect nano-sized mineral particles.
Mineralization has been assumed to be highly dependent on the nature of the surface. A number of polymer materials was selected for mineralization experiments. The selected organic polymers are common
in membrane technology and water filtration systems, namely polysulfone and poly(p-phenylene-oxide).
Polystyrene has been added as a common material in technology. In order to observe the smallest possible nano-crystals at a polymer surface the Raman scattering of the crystals must be of the some order of
magnitude as the Raman scattering from the organic layer. It was therefore decided to prepare very thin
polymer films with a thickness of the order of nanometers as part of the microfluidic device.
Finally, a model super saturated mineralization solution was prepared to understand early phenomena
occurring in solution. The solution was investigated by a double pulse experiment, which enables to assess
the mineralization rate and gives insight in the nature of pre-nucleation prior to a mineralization process.
A model mineralization solution has a well-defined metastable region which depends on parameters, such
as: super- saturation ratio, pH , ionic strength, temperature.
Knowledge gathered from the double pulse experiment will help to better control in–situ detection of scaling performed by Raman imaging in microfluidics. In this way more insight may be acquired if nucleation
and mineralization take place at organic surface and in dependence on the choice of the organic phase.
74
Momentum and mass transport over a superhydrophobic bubble mattress: the
influence of interface geometry
Peichun Amy Tsai, A. Sander Haase, Elif Karatay, and Rob Lammertink
Soft-matter, Fluidics and Interfaces Group, MESA+ Institute for Nanotechnology, University of Twente, The Netherlands
Website: www.tnw.utwente.nl/sfi & www.patsai.com/web
We numerically investigate the influence of interface geometry on momentum and mass transport on a
partially slippery bubble mattress. The bubble mattress, forming a superhydrophobic substrate, consists
of an array of slippery (shear-free) gas bubbles with (no-slip) solids walls in between. We consider pressure-driven laminar flow over the bubble mattress, with a solute being supplied from the gas bubbles. The
results show that solute transport can be enhanced significantly due to effective slippage, compared to a
fully saturated no-slip wall. The enhancement depends on the interface geometry of the bubble mattress,
i.e. on the bubble size, protrusion angle, and surface porosity. In addition, we demonstrate that the mass
transfer enhancement disappears below a critical bubble size. The effective slip vanishes for very small
bubbles, whereby interfacial transport becomes diffusion dominated. For large bubbles, solute transport
near the interface is greatly enhanced by convection.
References
1. E. Karatay et al., Proc. Natl. Acad. Sci. USA 110, 8422 (2013).
2. A. S. Haase et al., Soft Matter, 9, 8949 (2013).
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75
TEMPERATURE EFFECTS ON ENERGY PRODUCTION BY SALINITY EXCHANGE
Silvia Ahualli, María M. Fernández, Guillermo Iglesias, María L. Jiménez, Ángel V. Delgado*
Department of Applied Physics, Faculty of Science
University of Granada, 18071 Granada, Spain
In recent years, the capacitance of the interface between charged electrodes and ionic solutions (the
electrical double layer, EDL) has been increasingly investigated as a source of clean energy from salt concentration changes [1-3]. Charge is placed on the electrodes either by means of ion-exchange membranes
(CDP or Capacitive energy extraction based on Donnan Potential) or of an external power source (CDLE or
Capacitive energy extraction based on Double Layer Expansion). In the latter method, net energy is produced by simple solution exchange in open circuit (Fig. 1),. In this communication, we propose to explore the
changes in capacitance associated to temperature variations as well: a temperature increase produced a
decrease in EDL capacitance and hence a cycle is possible in which some charge is put on the electrodes
at a certain potential, and returned at a higher one (Fig. 1). There is also the possibility of gaining energy
from the so-called thermal membrane potential: an electric potential is generated when hot and cold
waters are contacted with anion and cation exchange membranes, respectively [4]. DLE technique from
the exchange of cold and warm waters (double layer permittivity exchange, DLPE) successively in contact
with charged electrodes. Furthermore, we will demonstrate, both theoretically and experimentally, that
temperature and salinity variations can be suitably combined (charging the electrodes in cold sea water,
and discharging them in warm fresh water) to maximize the potential increase and the energy available.
References
1. Brogioli, D. Phys. Rev. Lett. 2009, 103, 058501.
2. Brogioli, D.; Zhao, R.; Biesheuvel, P. M. Energy Environ. Sci. 2011, 4, 772–777.
3. Bijmans, M.; Burheim, O.; Bryjak, M.; Delgado, A.; Hack, P.; Mantegazza, F.; Tenisson, S.; Hamelers, H. Energy Procedia 2012, 20,
108 – 115.
4. Sales, B. B. Capacitive Technology for Energy Extraction from Chemical Potential Differences (ISBN: 978-94-6173-738-0). Ph.D.
thesis, Univ. Wageningen, The Netherlands. 2013.
Acknowledgements
The research leading to these results received funding from the European Union 7th Framework Programme (FP7/2007-2013) under
agreement No. 256868.
450
20 mM
600 mM
300
(mV)
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[email protected]
150
0
0
10
20
30
40
-3
QV (C cm )
Figure 1. Left: The CDLE process; center: a typical charge-discharge cyle; right: DLPE and CDLE compared in experimental conditions. Here we demonstrate that it is feasible to gain net energy in the C
76
Functionalized activated carbon for “capacitive mixing” energy production
Lorenza Misuri1, Massimo Marino1, Doriano Brogioli1, Silvia Ahualli2, Maria del Mar Fernandez2,
Guillermo Iglesias2, Angel Delgado2, Oleksandr Kozynchenko3
1 University of Milano-Bicocca, Italy
2 University of Granada, Spain
3 Mast Carbon, UK
The “capacitive mixing” (CAPMIX) technique for the energy production can be
considered the reverse of CDI. In the simplest case, the so-called “capacitive double
layer expansion” (CDLE) technique, we exploit the increase of the electrostatic
energy of an electric double layer, that takes place when the concentration of the
solution is reduced, resulting in the diffusion of the ions against the electric force.
The electric double layers must be already present when the concentration is changed; they
are usually generated by charging the electrodes by means of an external power supply. Now we
report experiments in which the double layers are obtained by chemical means:
charged functional groups are added to the surface of the activated carbon. This leads
to the spontaneous formation of an electric double layer, without the need of an external
device for charging the electrodes. We show that this approach leads to stable and repeatable
performances of the electrodes, with a power production of the order of 100 mW per square
meter of electrode.
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77
Ultrathin metal oxide coated mesoporous carbon material for enhanced capacitive
deionization
Sangho Chung1, Trinh Ngoc Tuan1, Jae Kwang Lee2, Jaeyoung Lee1, 2*
Electrochemical Reaction and Technology Laboratory (ERTL),
1
Ertl center for Electrochemistry and Catalysis,
2
Gwangju Institute of Science and Technology (GIST), Korea
Corresponding Author, email: [email protected]
Currently, capacitive deionization (CDI) has attracted attention as a low energy consumption and environmentally friendly desalination technique, because it can be conducted at low voltages without secondary
waste. In this work we have synthesized mesoporous carbon coated with ultrathin metal oxide via atomic
layer deposition (ALD) technique and used as CDI electrodes. The influence of ultrathin metal oxide on
the mesoporous carbon was studied to the CDI performance. It was identified from TEM, XRD, BET and
XPS that the mesoporous carbon was coated successfully by means of ALD method. As a results of cyclic
voltammetry and impedance, it was identified that metal oxide coated mesoporous carbon electrode has
more enhanced electric double layer capacitance and less diffusion resistance than previous carbon materials. Also charge-discharge and ion conductivity profiles showed that the ion removal ratios of metal oxide
coated mesoporous carbon electrode more than that of previous carbon electrode. In conclusion, carbon
electrode which was coated by ultrathin metal oxide with its high surface area and high dielectric constant
shows potential for CDI electrode material more effective than previous carbon electrode in CDI system.
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*
78
Mesoporous carbon nanofiber fabrication and its capacitive desalination application
Jianyun Liu, Shiping Wang, Le An, Haojie Pan, Miao Lu
College of Environmental Science and Engineering, Donghua University, Shanghai 201620, China
1. Y. Oren, Desalination , 228, 10–29 (2008)
2. J.C. Farmer, D.V. Fix, G.V. Mack, R.W. Pekala and J.F. Poco, J. Appl. Electrochem. 26, 1007-1018 (1996).
3. M. T. Z. Myint and J. Dutta, Desalination, 305, 24–30 (2012)
4. L. Pan, X. Wang, Y. Gao, Y. Zhang, Y. Chen and Z. Sun, Water Res., 244, 139–143 (2009)
5. C. Kim, B.T.N. Ngoc, K. S. Yang, M. Kojima, Y. A. Kim, Y.J. Kim, M. Endo and S.C. Yang, Adv. Mater., 19, 2341–2346 (2007)
6. Z-M. Huang, Y-Z. Zhang, M. Kotaki and S. Ramakrishna, Comp. Sci. Tech., 63, 2223–2253 (2003)
7. D. Lai and Y. Xia, Adv. Mater., 16, 1151-1170 (2004)
8. J. B. Donnet and R. C. Bansal, Carbon Fibers, Marcel Dekker, New York (1990)
9. C. Kim and K. S. Yang, Appl. Phys. Lett., 83, 1216-1218 (2003)
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References
Tuesday
The lack of fresh water is one of the most serious problems for human beings in the 21st century. In
order to generate fresh water from sea water and brackish water, various desalination methods, such
as distillation, electrodialysis, reverse osmosis, activated carbon adsorption and ion exchange method
have been developed for water desalting. Capacitive deionization (CDI) technology is recently becoming
increasly attractive as an alternative desalination method due to low energy consumption and needless
of chemicals[1-2]. CDI is referred to an electrosorption process, in which ions in water are adsorbed in the
electrical double layer when electrodes are charged, and then desorbed when electrodes are discharged.
At the same time, the electrode is regenerated. Because the voltage applied between the positive and
negative electrodes in CDI cell is lower than that of water electrolysis(< 1.2V), water electrolysis is avoided
and much energy saved[3]. Therefore, it is a very promising technology for water desalination nowadays.
The high capacitive and high conductive electrode materials are needed in order to enhance the accumulation of ions and decrease energy consumption, respectively. A high capacitive material should have a
high surface area for ion accumulation. Recently, the high porous and conductive carbon based materials,
such as carbon aerol gel[2], carbon nanotube[4] and carbon fiber[5] have been developed in order to increase the desalination capacity of the electrode materials.
Electrospun technique is very suitable for carbon nanofiber material fabrication with 100-500nm diameter[6]. The electrostatic force between the tip and collector electrode drives the fiber formation of a polymer solution. One of the most used polymer is polyacrylonitrile (PAN) due to its good spinnability in solution[7] and its relatively high carbon yield.[8] The resultant PAN-based carbon fiber has high surface area
and tunable porous structure after suitable activation by steam activation or CO2 activation[9]. These physical activation processes were difficult to control the pore size and the porous carbon fibers were easily
deactivated with recycling. In this report, we present our strategy to get the self-sustainable mesoporous
electrospun carbon fiber by adding some chemicals such as polymethyl methacrylate (PMMA) or polystyrene (PS) in the electorspun polymer precursor solution as a pore-forming component. BET analysis,
SEM and electrochemical characterization were made to understand the porous structure and capacitive
properties. The pore size and density can be tuned by adjusting the ratio of the additives. The mesopores
with 10-50 nm pore size were formed at the ratio of PAN/PMMA of 4:1. Cyclic voltammetry experiment
confirmed that the specific capacitiance of the carbon fiber has a significant increase compared with the
pure PAN drived carbon fiber. The capacitive desalination performance was investigated by assemblying
the self-sustainable mesoporous fiber electrode in the capacitor. The salt adsorption capacitance was 6.5
mg/g and 7.5 mg/g corresponding to PAN/PS and PAN/PMMA drived carbon fiber electrode, respectively.
Both are much higher than that of the pure PAN drived carbon fiber (2.3 mg/g). The stability test was
measured. It demonstrates that the mesoporous carbon fiber electrode is potential for water softing and
brackish water desalination application.
CDI carbon electrode coated with ion selective layer
Namsoo Park, Kyungseok Kang, Wonkeun Son
Institute of technology, siontech. co. ltd.
530 Yongsandong, Yuseong-gu, Daejeon, Korea
Capacitive deionization (CDI) is an ion removal technology based on storing ions in the polarization layers
of two oppositely charged electrodes. CDI process is defined as a potential driven adsorption of ions onto
a charged electrode surface. CDI is a technology similar to that of electric double layer (EDL) super-capacitors but modified to operate in a flow through system. Conventional CDI is known to be energy inefficient because of the dissolved salt present in the pore volume of the carbon electrode. When an electric
potential is applied, counter-ions in the pore adsorb onto the electrode and co-ions are expelled from the
electrodes. So ion adsorption and desorption occur simultaneously in the surface of electrode, seriously
reducing desalination efficiency. To solve this problem, a charge barrier should be placed near to the electrode of CDI[1]. It is called membrane-capacitive-deionization (MCDI) in which very expensive ion exchange membranes are used. So, we have developed novel CDI electrode coated with very thin ion exchange
layer, which is shown in the Fig. 1. This CDI electrode leads to have very low resistance, to enhance the salt
removal performance and to lower its production cost[2].
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Fax : +82-(42)-935-0405, E-mail address : [email protected]
Fig. 1. SEM image of the cross section of ion selective layer coated CDI electrode.
References
1. Andelman, M. D., Charge barrier flow-through capacitor, CA patent 2444390, (2002).
2. Kyung-Seok Kang, et al., Manufacturing Method of Electrode, KR patent 1010473350000, (2008).
80
Keynote
Dynamics of metal uptake by biointerfaces
Jérôme F. L. Duval
CNRS-Université de Lorraine, LIEC (Laboratoire Interdisciplinaire des Environnements Continentaux),
UMR7360, Vandoeuvre-lès-Nancy F-54501, France.
* [email protected] ( http://duvaljfl.webnode.fr/)
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References
Tuesday
In this presentation, a formalism for the dynamics of uptake of metal ions by microorganisms is discussed.
The theory integrates the interplay over time between metal depletion in bulk solution, metal adsorption
at the microbial interphase, metal excretion (efflux) and transport of metals by conductive diffusion toward the metal-consuming biomembrane. The model further involves basic physicochemical descriptors
of the microorganism in terms of size, interfacial distribution of electrostatic charges, or thickness of peripheral soft surface appendage. A generalization of the Best equation1 is proposed and rationalizes the
evolution over time of the concentration of metal ions at the active membrane surface as a function of
bulk metal concentration. Combination with metal conservation condition over the sample volume allows
a full evaluation of bulk metal depletion kinetics and the accompanying time-dependent uptake and excretion fluxes as a function of metal-microorganism electrostatic interaction, microbe concentration and
relevant biophysicochemical features of the interphase. Practically tractable expressions are derived in the
limit where the Biotic Ligand Model (BLM) is obeyed and in situations where conductive diffusion transport of metals significantly determines the rate of biouptake. In particular, the plateau value reached at
sufficiently long times by bulk metal concentration is rigorously expressed in terms of the key parameters
pertaining to the adsorption process and to the kinetics of metal uptake and excretion. The theory extends
and unifies previous models2-4 where the impacts of extracellular metal transport and/or metal efflux on
the overall rate of biouptake were ignored. At the end of the presentation, few elements will be provided
on ongoing modelling of metal biouptake in metal-complexing media and under conditions where microbial growth kinetics contribute to the dynamic partitioning of metals across biointerphase.
1. J. B. Best, Cell Comp. Physiol., 1955, 46, 1-27.
2. J. P. Pinheiro, J. Galceran and H. P. van Leeuwen, Environ. Sci. Technol., 2004, 38, 2397-2405.
3. R. Hajdu, J. P. Pinheiro, J. Galceran, V. I. Slaveykova, Environ. Sci. Technol., 2010, 44, 4597-602.
4. J. F. L. Duval, Phys. Chem. Chem. Phys., 2013, 15, 7873-7888.
81
Validity of the Boltzmann equation to describe Donnan equilibrium at the MembraneSolution Interface
A.H. Galama,a,b J.W. Post,a, c M.A. Cohen Stuart,d and P.M. Biesheuvel,b
aDepartment of Environmental Technology, Wageningen University, Bornse Weilanden 9, 6708 WG Wageningen, The Netherlands.
bWetsus, centre of excellence for sustainable water technology, Oostergoweg 7, 8911 MA Leeuwarden, The Netherlands. cKWR Watercycle Research Institute, Groningenhaven 7, 3433 PE Nieuwegein, The Netherlands. dDepartment of Physical Chemistry and Colloid
To describe Donnan equilibrium at the membrane-solution interface, the simplest approach uses the classical Boltzmann equation, based on a mean-field description of ions as ideal point charges, in combination
with the assumption of fully overlapped electrical double layers in the membrane pores. We test the Boltzmann equation by measurement of the equilibrium counterion and co-ion concentration in densely charged membranes equilibrated with various NaCl solutions (0.01-3 M). To obtain a good fit of data it was
found necessary to express the membrane charge and ion concentrations per volume of aqueous solution
phase in the membrane, and to include a small energetic term in the Boltzmann relation. A discrepancy
between theory and experiment data is found at low external NaCl concentrations. Similar deviations from
the Donnan model have been reported for over half a century, but do not yet have a convincing explanation. Agreement between experiment data and theory at low external NaCl concentrations is obtained
when we model the desorption experiment taking into account the role of H+ and OH- ions in closing the
charge balance, and postulating the presence in the membrane of a tiny amount of fixed groups with a
charge opposite to overall fixed membrane charge.
References
1. Galama et al., J. mem. sci. 442 (2013) 131-139
8
counterions
cions,membrane (M)
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Science, Wageningen University, Dreijenplein 6, 6703 HB Wageningen, The Netherlands.
6
4
2
co-ions
0
0
82
1
2
cNaCl,external (M)
3
Ion-Exchange Membrane
Recent advances in diffusive gradients in thin films (DGT). The role of electrostatic
effects and dissolution of metal nanoparticles.
J. Puy, S. Cruz-González, C. David, C. Rey-Castro and J. Galceran*.
Department of Chemistry, Universitat de Lleida & AGROTECNIO, Av. Rovira Roure 191, 25198 Lleida, Spain
*E-mail contact: [email protected]
1. W.Davison, H.Zhang, Nature 367 (1994) 546.
2. S.Mongin, R.Uribe, J.Puy, et al. Environ. Sci. Technol. 45 (2011) 4869.
3. J.Puy, R.Uribe, S.Mongin, et al. J. Phys. Chem. A 116 (2012) 6564.
4. M.Alfaro-De la Torre, P.Y.Beaulieu, A.Tessier, Anal. Chim. Acta 418 (2000) 53.
83
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References
Tuesday
DGT [1] is a widely used technique for measuring metal fluxes in environmental systems, especially aquatic
media. In a DGT device, metal is accumulated in the beads of a resin dispersed in a gel (forming the resin
layer). Metal ions arrive to the resin after crossing a diffusive layer of just gel. Metal complexes moving
through the diffusive gel can penetrate into the resin layer [2,3]. This penetration of complexes into the
resin layer usually enhances the accumulation, because their dissociation proceeds at maximum speed
and, so, acts increasing the lability of the complexes in comparison with other sensors where the detection
proceeds just in a surface (and not in a volume, like in DGT).
An adequate knowledge of the dissolution of inorganic nanoparticles (NPs) is key for understanding the
environmental and toxicological impact of these materials. DGT yields an estimation of the labile fraction
of metal dissolved from ZnO nanoparticles in aqueous dispersion without any prior solid/liquid separation
step. The results show the relevance of pH and metal speciation in the aqueous phase on the measured
labile fractions.
Electrostatic effects, due to the electrical charges of the resin beads, dramatically impact on the penetration of complexes into the resin disc. For decreasing ionic strengths, negatively charged complexes will
experience stronger electrostatic repulsion from the resin layer leading to a reduction of the accumulated
mass, while positively charged complexes will contribute to enhanced metal accumulations. Experimental
evidences of this behaviour will be shown for Ni, Cd and Co complexes with nitrilotriacetic acid (NTA) and
ethylenediamine (Etdiam). A simple electrostatic model quantitatively explains the results. By fitting the
experimental accumulations, one obtains values of the Boltzmann factors which can be used in other
systems. These effects are extremely important for a correct interpretation of DGT measurements in pristine waters, such as lakes [4]. Moreover, the increased kinetic dissociation constant in the resin domain (in
comparison to the Eigen value in the gel domain) is an important phenomenon that supports the classical
interpretation of DGT sensing mostly the labile species.
Capacitive Response of PDMS-coated IDE Platforms Directly Exposed to Aqueous
Solutions Containing Volatile Organic Compounds
Judith Staginus1,2, Isabelle M. Aerts1, Zu-Yao Chang3, Gerard C.M. Meijer3, Ernst J.R. Sudhölter1
Louis C.P.M. de Smet1
1
TU Delft, Department of Chemical Engineering, Organic Materials & Interfaces, The Netherlands
2
Wetsus, Centre of Excellence for Sustainable Water Technology, The Netherlands
3
TU Delft, Department of Micro-electronics and Computer Engineering, Electronic Instrumentation Laboratory, The Netherlands
Surface-engineering of micro- and nanostructured transducer platforms with different chemical layers is
gaining increasing interest for bio-medical and environmental sensing applications, including water quality
monitoring. Polymer-coated interdigitated electrodes (IDEs) have shown great potential for the capacitive
detection of volatile organic compounds (VOCs) not only in air, but also in water using headspace techniques [1,2]. The application of polymers with different affinities towards different VOCs onto the individual
spots of an IDE multi-array allows to one to obtain a (capacitive) fingerprint of contaminated water, which
can subsequently be analysed with pattern recognition tools. However, headspace technology is an indirect detection method as measurements are performed in the gas phase that is in equilibrium with the
aqueous pollutant solution.
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Email: [email protected]; Web: http://www.cheme.nl/omi/
Figure 1. (left) Schematic overview of a polymer-coated IDE applied directly in water and (right) the reversible capacitive response of a PDMS-modified IDE platform to MTBE in water.
The aim of our research is to measure and understand the capacitive response of polymer-coated IDE
platforms directly exposed to aqueous solutions containing VOCs [3,4]. Here, we present on the capacitive sensor response of polydimethyl siloxane (PDMS)-coated, micro-sized IDEs of gold when exposed to
an aqueous environment spiked with different VOCs, including methyl tert-butyl ether (MTBE), toluene,
m-xylene, benzene and n-hexane. The capacitive response changes upon absorption of the VOCs in the
polymer layer are in line with their i) polymer affinity and ii) relative dielectric constants as compared to
the one of thin PDMS layers. In addition, the response changes were fully reversible. Different aspects
related to the application of polymer-coated IDEs directly in water as compared to gas-phase analysis will
be discussed. This will include the so-called third electrode effect and the analysis of salt solutions.
References
1. Hagleitner, C.; Hierlemann, A.; Lange, D.; Kummer, A.; Kerness, N.; Brand, O.; Baltes, H. Nature 2001, 414, 293–296.
2. Igreja, R. and Dias, C.J. Sensors and Actuators A: Physical 2004, 112, 291–301.
3. Staginus, J.; Aerts, I.M.; Chang, Z.-Y.; Meijer, G.C.M.; de Smet, L.C.P.M.; Sudhölter, E.J.R. IMCS 2012 - The 14th International Meeting on Chemical Sensors, Nürnberg (Germany), May 20-23, 2012. pp 1141–1144.
4. Staginus, J.; Aerts, I.M.; Chang, Z.-Y.; Meijer, G.C.M.; de Smet, L.C.P.M.; Sudhölter, E.J.R. Sensors & Actuators, B: Chemical 2013,
184, 130-142.
84
Keynote
The Importance of Carbon Electrode Material Affecting
the Maximum Deionization Performance in CDI Process
Taeyoung Kim and Jeyong Yoon*
School of Chemical and Biological Engineering, Institute of Chemical Processes,
Seoul National University, Daehak-dong, Gwanak-gu, Seoul 151-742, Republic of Korea
mail; [email protected]; http://env.snu.ac.kr
Water shortage problem is a global environmental issue today. Desalination can provide a solution to
water scarcity and subsequent increasing freshwater demands in agriculture, industry, and household.
Recently, capacitive deionization (CDI) has attracted growing attention as a novel desalination technology.
CDI produces deionized water while saline water passes between closely-packed electrodes upon charging, in which porous carbon materials play an important role to achieve an effective desalination. Therefore, various carbon materials, such as carbon aerogel, ordered mesoporous carbon, and carbide-derived
carbon, have been investigated as CDI electrodes to provide improved desalination performance. Previous
studies have reported that the desalination performance in terms of deionization capacity (or salt adsorption capacity) was significantly affected by types of carbon material. In this presentation, we will show
how importantly the deionization performance is affected by carbon electrode materials including their
deionization capacity, especially focused on properties of carbon electrodes.
Tuesday
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85
Insight into the electrochemical property of TiO2/AC electrodes prepared by a
microwave-assisted ionothermal synthesis method for capacitive deionization
Li-Ching Chung*, Po-I Liu, Min-Chao Chang, Hsin Shao, Chia-Hua Ho, Teh-Ming Liang, Ren-Yang Horng
Material and Chemical Research Laboratories, Industrial Technology Research Institute (ITRI), Bldg. 17, 321, Sec. 2, Kuang Fu Road,
Hsinchu 30011, Taiwan
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*Email: [email protected]
Four nanostructured anatase titanium dioxide (TiO2)/ activated carbon (AC) composite materials for capacitive deionization electrodes were prepared by a two-step microwave-assisted ionothermal (sol-gel
method in the presence of ionic liquid) synthesis method. It includes a reaction and a crystallization step.
In the crystallization step, the ionic liquid plays a hydrothermal analogy role in driving the surface anatase
crystallization of amorphous TiO2 nanoparticles formed in the reaction step. The electrochemical property
of these composite electrodes was investigated.
In general, the electrode prepared from the AC material with highly hydrophilic surface would have high
specific capacitance. It was also reported that the specific capacitance of activated carbon electrode was
enhanced after the modification of nanostructured anatase titanium dioxide. However our results found
out that the effect of TiO2 on the specific capacitance of nanostructured anatase TiO2/ AC composite is dependent on the characteristics of pristine AC, especially for the pore size and the hydrophilicity in our study system. It may be a positive effect or negative effect. The negative effect was observed in the case of AC
material with micropores and highly hydrophilic surface. These effects will be investigated and discussed
using multiple techniques, including X-ray spectroscopy, thermogravimetry analysis, cyclic voltammetry,
electrochemical impedance spectroscopy, etc.
References
1. P.I. Liu, L.C. Chung, H. Shao, T.M. Liang, R.Y. Horng, C.C.M. Ma, M.C. Chang, Electrochimica Acta 96 (2013) 173.
2. R.E. Morris, Chemical Communications 7 (2009) 2990.
3. M.K. Seo, S.J. Park, Current Applied Physics 10 (2010) 391.
86
Vertically-Aligned Carbon Nanotube Electrodes for Capacitive Deionization
H. K. Mutha1, R. Mitchell2, R. Enright1,3, C. V. Thompson2, and E. N. Wang1
1Department of Mechanical Engineering, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts, 02139, U.S.A.
2Department of Materials Science, Massachusetts Institute of Technology, 77 Massachusetts Avenue, Cambridge, Massachusetts,
02139, U.S.A.
3Stokes Institute, University of Limerick, Limerick, Ireland
Email: [email protected], [email protected]
1. S. Porada et al., “Review on the science and technology of water desalination by capacitive deionization”, Progress in Materials
Science, vol. 58, pp 1388-1442, Oct 2013.
2. R. Cross et al., “A metallization and bonding approach for high performance carbon nanotube thermal interface materials,”
Nanotechnology, vol. 21, p. 445705, Dec. 2010.
3. P. M. Biesheuvel and M. Z. Bazant, “Nonlinear dynamics of capacitive charging and desalination by porous electrodes,” Physical
Review E, vol. 81, p. 031502, Mar 2010.
Figure 1. Synthesized VA-CNT electrodes. a) Scanning
electron microscope images of transferred CNTs, b)
CNT carpet transferred onto corrosion-resistant substrate.
Figure 2. Charging time constant of CNT electrodes
for varying heights and sodium chloride solution
concentrations. Potentiostatic measurements were
taken in a 3-electrode cell.
87
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References
Tuesday
We investigated the role of porous geometry using vertically-aligned carbon nanotube (VA-CNT) electrodes in capacitive deionization (CDI). CDI promises to be an efficient and compact means to achieve water
desalination through adsorption of ions on high surface area electrodes. In order to optimize salt adsorption in CDI, an improved understanding of electrode properties, such as optimal pore size and electrode
thickness for ion removal [1], is desired. Current studies typically use highly porous, tortuous electrode
materials, which complicates the ability to obtain detailed understanding of salt adsorption and charging
dynamics. In this work, we designed and synthesized VA-CNT electrodes to investigate the role of height
and spacing on salt adsorption rates. The VA-CNTs were synthesized using chemical vapor deposition with
inner and outer diameters of 5.6 nm and 7.7 nm, respectively, and heights of 20 to 600 μm, with specific
surface areas of 540 m2/g. These VA-CNTs were transferred onto a corrosion-resistant electrode using
Au-Au thermocompression bonding [2] (Figure 1). We first characterized the capacitance and charging
dynamics with a three-electrode test cell in sodium chloride solution. The material capacitance ranged
from 20-40 F/g in NaCl solutions of varying concentrations from 15-1000 mM, respectively. The charging
time constants were extracted from the potentiostatic data (Figure 2), which indicate that the time constant varies linearly with the height of the carpet and is proportional to the Debye length. These results
suggest that the charging effect is due to charge storage in the double layer and surface conduction in the
CNTs. These effects may be due to the mesoporous nature of the CNT carpets. In addition, we are currently
investigating the VA-CNTs in a flow through test cell, where we can correlate the results from the potentiostatic measurements to ion removal for desalination. These results offer a first step towards improved
understanding of porous electrode geometries for CDI.
The Influence of Heteroatom Doping of Porous Carbon
on the Salt Adsorption Capacity and Kinetics in Capacitive Deionization
Florian Schipper,1,* Tim-Patrick Fellinger,1 Gerard Sans, 2 Slawomir Porada,2 Daniel Weingarth,2
Volker Presser,2,3 Markus Antonietti1
1 Max Planck Institute of Colloids and Interfaces, Colloids Department, Am Mühlenberg 1, 14476 Potsdam, Germany, http://www.
mpikg.mpg.de/en
2 INM – Leibniz Institute for New Materials, Campus D2 2, 66123 Saarbrücken, Germany, http://www.inm-gmbh.de & http://www.
presser-group.com
3 Saarland University, Campus D2 2, 66123 Saarbrücken, Germany, www.uni-saarland.de
*Email address: [email protected]
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Key words: Porous Carbons, Salt Templating, Nitrogen-Doped, Sulfur-Doped
The production of potable, deionized water is a major challenge and capacitive deionization (CDI) has
gained increased attention over the last years as an energy efficient alternative to reverse osmosis or ion
exchange technologies for desalination of brackish water. Since CDI is based on the same phenomenon
of ion electroadsorption as electrical double layer capacitors, porous carbons in general and activated
carbons in particular are of interest and importance to CDI as they combine high surface area and low manufacturing costs with high availability. Various fabrication techniques (e.g., carbide-derived carbons, physical or chemical activation of biomass etc.) can be used to produce porous carbon materials. Especially
the carbide-derived carbons are of great importance to understand the impact of the pore size distribution
on the CDI process[1].
In our study , for the first time, we apply salt templated carbons for water desalination using CDI with
a high surface area and pore volume derived via simple solution based bottom-up process allowing to
produce porous carbons from glucose. Zinc chloride was used as a salt template to introduce porosity[2].
By careful adjusting the ZnCl2 to glucose ratio the morphology can be tuned from a microporous to a
mesoporous material. The resulting carbon material can be easily doped with sulfur or nitrogen by adding
soluble precursors or changing the carbon source to glucosamine. Both, the impact of these heteroatoms
and the details of porosity and pore size distribution on the overall CDI performance and salt adsorption
kinetics will be presented and compared with the validity of the CDI predictive tools published in Ref. [3].
References
1. Porada, S., et al., Review on the science and technology of water desalination by capacitive deionization. Progress in Materials Science, 2013. 58(8): p. 1388-1442.
2. Fechler, N., T.-P. Fellinger, and M. Antonietti, “Salt Templating”: A Simple and Sustainable Pathway toward Highly Porous Functional Carbons from Ionic Liquids. Advanced Materials, 2013. 25(1): p. 75-79.
3. Porada, P., et al., Direct Prediction of the Desalination Performance of Porous Carbon Electrodes for
Capacitive Deionization, Energy and Environmental Science, 2013. 6(12): p. 3700-3712.
88
Characterization of Internal Resistance for Capacitive Deionization Systems
Yatian Qu, 1 Juan G. Santiago, 1 Michael Stadermann2
1 Department of Mechanical Engineering, Stanford University,
440 Escondido Mall, Stanford, CA, USA. Website: http://microfluidics.stanford.edu/
2 Lawrence Livermore National Laboratory, 7000 East Avenue, Livermore, CA, USA
Email: [email protected], [email protected], [email protected]
References
1. Porada, S.; Zhao, R.; van der Wal, A.; Presser, V.; Biesheuvel, P. M. Progress in Materials Science 2013, 58, 1388-1442.
Tuesday
Current CDI devices consume significantly more energy than the theoretical thermodynamic minimum.1
One significant energy cost pathway is power dissipation through the internal resistance of CDI cell during
charging and discharging. Therefore, understanding the contributions to resistance in CDI systems is critical for developing high performance devices. We are working to fully characterize resistive components
and associated energy costs in CDI systems with the goal of reducing those resistances and developing low
energy consumption devices. Internal resistance in CDI systems consists of ohmic resistance in materials,
solution resistance and charge transfer resistance.2 Figure 1 shows the resistive components in a typical
CDI cell. All these components contribute to energy dissipation in charging and discharging process. We
designed a custom four-probe measurement platform to measure resistivity of porous electrodes and
characterize contact resistance between electrodes and current collectors under various operation conditions. We used electrochemical impedance spectroscopy (EIS) and galvanostatic charge–discharge tests
to perform measurements. Our characterization is based on using carbon aerogel monoliths (HCAMs)3 as
electrodes and several common carbon or metal materials as current collectors. Our preliminary results
demonstrate that charge transfer resistance can be reduced by applying compression force on electrodes
and current collectors (Figure 2). Other affecting parameters may include porous electrodes materials,
current collector materials and feed solutions.
2. Lei, C.; Markoulidis, F.; Ashitaka, Z.; Lekakou, C. Electrochimica Acta 2013, 92, 183-187.
3. Baumann, T. F.; Worsley, M. A.; Han, T. Y.-J.; Satcher, J. H. Journal of Non-Crystalline Solids 2008, 354, 3513-3515.
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Figure 1. Resistive components in a CDI
Figure 2. Reduced charge-transfer resistance by electrodes
cell
compression
89
Protein humic acid interaction
Tuesday
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L. K. Koopala, W. F. Tanb, Y. Lib, W. Nordea
a
Laboratory of Physical Chemistry and Colloid Science, Wageningen University, Dreijenplein 6, 6703 HB Wageningen, The Netherlands
b
College of Resources and Environment, Huazhong Agricultural University, Wuhan 430070, China.
In the natural environment of aqueous solutions and soil solutions proteins can form complexes with the
natural dissolved organic matter. Humic acid (HA) is an important component of the dissolved organic
matter. On the basis of results obtained for the humic acid (HA) - lysozyme (LSZ) system, the interactions
between proteins and HA will be discussed together with their effect on the activity of the protein. In solution LSZ is positively charged and HA is negative at the investigated pH values; the discussion is relevant
for other HA–protein systems when the protein is positively charged.
The charge of the HA/LSZ complexes at the IEP in the presence of KCl is compensated for 30 – 50 % by K+;
depending on pH and KCl concentration. Dynamic light scattering measurements reveal that complexation
of HA with LSZ starts as soon as HA is added to LSZ and is followed by aggregation when the iso-electricpoint (IEP) of the complexes is approached. Aggregation is gradual for 50 mM KCl and sudden for low KCl
concentrations. The aggregate size is at its maximum at the IEP of the complexes. At mass ratios beyond
the IEP the aggregates partially disaggregate. Calorimetry indicates that binding of LSZ to HA is initially
enthalpically driven. Near the IEP complexation and aggregation are due to hydrophobic forces (structural
re-organization) and counterion release.
The enzyme activity of LSZ decreased upon complexation with HA and the decrease of the enzyme activity
increased by subsequent aggregation. A critical HA/LSZ mass ratio for the behavior of the enzyme activity
was that at the IEP of the complex. Before this mass ratio was reached the LSZ activity strongly decreased
under all conditions. Beyond this mass ratio both pH and ionic strength affected the activity of LSZ in the
complex.
90
A biophysicochemical approach for assessing the dynamics of metal uptake by
microorganisms
E. Rotureau1,2*, P. Billard1,2, J.F.L Duval1,2
1 CNRS, LIEC (Laboratoire Interdisciplinaire des Environnements Continentaux),
UMR7360, Vandoeuvre-lès-Nancy F-54501, France.
2 Université de Lorraine, LIEC, UMR7360, Vandoeuvre-lès-Nancy, F-54501, France.
* email address: [email protected]
Laboratory website: http://liec.univ-lorraine.fr/
1. Galceran J. and van Leeuwen H.-P. (2004), in Physicochemical kinetics and transport at biointerfaces, eds H. P. van Leeuwen and
W. Köster, John Wiley, Chichester, Chapter 4, pp. 147.
2. Hadju R., Pinheiro, J.-P., Galceran, J., Slaveykova, V.I. (2010) Modeling of Cd uptake and efflux kinetics in metal-resistant bacterium Cupriavidus metallidurans, Environ. Sci. and Technol. 44, 4597-4602.
3. Duval J.-F.-L. (2013). Dynamics of metal uptake by charged biointerphases: bioavailability and bulk depletion. Physical Chemistry
Chemical Physics. 15, 7873-7888.
4. Duval J.-F.-L and Rotureau E. (submitted). Dynamics of metal uptake by charged biointerphases: impacts of depletion, internalization, adsorption and excretion. Physical Chemistry Chemical Physics.
91
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References
Tuesday
Understanding the toxic and essential trace compounds uptake by microorganisms in the conditions that
are the most relevant to the natural environment is a major trigger of concern in environmental risk
assessments. One of the scientific issues is to define metal bioavailability in the vicinity of a given biological surface taking into account the dynamic interplay between physicochemical properties of pollutants,
physiology of the exposed organisms, and prevailing environmental conditions. In addition, the different
mechanisms involved in metal uptake (e.g. metal transport, passive and active sorption, internalization,
possible excretion) may modify the metal bioavailability over the time [1,2]. In this context, the aim of
this work is to develop and to propose an experimental approach able to identify the biological and physicochemical parameters controlling the metal availability and uptake by a microorganism. To this end,
the time evolution of the metal depletion measured in-situ in bacteria suspension is considered as an
input toward a fine mechanistic description of the biouptake dynamics. The interpretation of metal depletion kinetics in solution is supported by a theoretical approach recently developed for the description
of the steady-state uptake flux of metallic ions at a charged and soft interphase of a microorganism [3,4].
The formalism provides useful information on the bio-physico-chemical processes at the bacteria-medium interphase governing metal uptake and metal bioavailability. The results that will be discussed in this
presentation are obtained for two strains of soil bacteria Pseudomonas putida: one is the wild strain able
to regulate metal ions and the other is devoid of efflux transporters. The time dependence of bulk metal
concentration in bacteria suspension is performed with advanced electroanalytical techniques. A relevant
set of metal depletion kinetic data is obtained for different volume fractions of bacteria cells. By means
of the general expressions recently derived for the depletion kinetics of metal ions from bulk solution, we
are able to describe the overall biouptake process dynamics and to evaluate the parameters pertaining to
sorption processes and kinetics of internalisation and excretion. In forthcoming studies, our experimental
approach will be extended to aquatic media containing metal-colloidal ligand mixtures.
Sorption of organic molecules on environmental sorbents: driving water molecules in
or out?
Mikhail Borisover
Tuesday
16.50 - 17.50
Rabobank zaal
Institute of Soil, Water and Environmental Sciences, The Volcani Center, ARO, Bet Dagan, Israel ([email protected])
Water at inorganic and organic surfaces and interfaces is well-known to affect physico-chemical and biological reactivities of environmental sorbents, such as, e.g., soils, sediments and aerosols. In this way,
water-sorbent interactions may control the environmental fate of multiple pollutants. Therefore, it is of
both basic and applied interest to learn how water-sorbent interactions may be affected by the presence
of sorbed organic molecules. Typically, this effect is difficult for quantification at environmentally relevant
low concentrations of organic molecules. However, this quantification may be possible by considering a
thermodynamic conversion of organic compound distribution coefficients Kd determined from a vapor
phase (or an inert solvent medium) at variable relative humidity RH (or water activity) into the derivative
describing the response in the sorbed amount of water molecules (nW) to the amount of a sorbed organic
compound (nA):
Further analysis of the relations between this differential effect and a structure of organic sorbates may
be carried out by using the linear free energy relationships. In the presentation, based on the literature
and own data on vapor and liquid phase sorption, this quantification is carried out for organic compounds
on (a) various mineral phases, such as quartz, metal oxides, clays, and (b) natural organic matter (NOM)
and humic acid, with the focus on complexed relationships between sorption of organic compounds and
water molecules on NOM. The demonstration of markedly different effects of “non-polar/hydrophobic”
vs. “polar/hydrophilic” organic sorbates on water associated with NOM is of special interest. So, sorbing
hydrophobic hydrocarbons drive water out of the bulk humic acid phase whereas hydrophilic organic compounds sorbed result in an enhanced hydration of this sorbent (Figure; the effect is differentiated by the
sign of the derivative). The effect of the enhanced hydration of the NOM sorbent (not observed typically
on inorganic phases) may be associated with participation of several water molecules thus giving rise to
“cooperativity” in water-NOM interactions, when several water molecules may (should) participate cooperatively in interactions with NOM but not in a stepwise manner. Notably, this cooperativity is induced by
sorbing organic molecules. The analysis of experimental data suggests also that the NOM hydration induced and enhanced at the presence of organic sorbates may occur also when NOM (in soils and sediments)
is assumed to be fully pre-hydrated by bulk water. Thus, when analyzing sorption of organic molecules
from water by NOM, the continuing process of NOM hydration, at the presence of organic sorbates, may
need to be included in considering the sorption mechanisms.
Organic sorbates:
"non-polar/hydrophobic"
"polar/hydrophilic"
5
4
3
2
nW 1
nA 0
-1
-2
-3
-4
0
10
20
30
40
50
60
70
80
90
Compound #
Vapor sorption on Leonardite humic acid
(in the 70-98% relative humidity range)
92
Comparison of Arsenic Adsorption on clays from Morocco
Yassine Bentahar a,b , Charlotte Hurela, Khalid Draouib ,Slimane Kairounb,Nicolas Marmiera
a Université Nice Sophia Antipolis, Laboratoire des Ecosystèmes Marins Côtiers et réponse aux stress (ECOMERS /EA4228), Facultés
des Sciences, Parc Valrose, 06108 Nice Cedex02,France.
b Université Abdelmalek Essaadi de Tétouan, Laboratoire de Chimie de l’Environnement, Faculté Des Sciences, avenue M’hanech,Tetouan Morocco.
[email protected]
Arsenic adsorbed en µg/g
400
350
300
250
200
150
100
50
0
1
2
3
4
5
6
7
8
9
10 11 12 13
pH
Figure 1: Effect of pH on the adsorption of Arsenic
93
16.50 - 17.50
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yellow clay
red clay
E clay
stevensite
450
Tuesday
In the recent years, growing concern for environmental issues have brought researchers of both analytical
and materials science to investigate appropriate processes for the removal and/or monitoring of various
pollutants. Among the pollutants, arsenic is one of the most toxic elements that can be found, as it is a
strong poison and a carcinogen. Unfortunately, it is released into the environment during many industrial
processes. Thus, the removal of arsenic from process solutions and effluents is necessary to protect the
environment.
The aim of this work is to study arsenic adsorption behavior onto clays from Morocco. Four clay samples
were investigated: red clay and yellow clay from Oued aou (Tétouan), E clay from Tetouan and stevensite
from the south-eastern border of the Tertiary basin of Missour.
Adsorption isotherms were conducted as a function of pH, and initial As concentration. Also the kinetics
of adsorption was investigated and FTIR, CEC, TOC, XRD measurements were performed on red and yellow
clays.
The effect of the pH on the adsorption of As for the 4 clays is shown in figure 1. From this result, arsenic
adsorption was most favorable in acid medium for red clay, yellow clay, and E clay. For stevensite, no significant adsorption was found in the whole pH range considered.
The kinetics experiments of adsorption of arsenic on the four clays were found to be comparable to a
pseudo-second –order model.
Langmuir and Freundlich isotherms were employed to describe the Arsenic adsorption in this clay. The
result obtained shown that these two models are favorable process of red clay and E clay. Furthermore, for
yellow clay and stevensite were correlated by the Langmuir and Freundlich models respectively.
The order of affinity of As toward the 4 clays was red clay> E clay> stevensite > yellow clay. This order of
affinity is explained by the presence of iron oxides (hematite) revealed by IR analysis of the solid in the
red clay. On the other hand, neither CEC nor TOC data allowed us to conclude about this order of affinity.
Attenuation of metal cations by iron oxide minerals from acid mine drainage
Arthur Baleeiro1, Saínza Arufe1, Juan Antelo2, Sarah Fiol1, Florencio Arce1
Department of Physical Chemistry and 2Department of Soil Science and Agricultural Chemistry, University of Santiago de Compostela,
1
15782 Santiago de Compostela, Spain.
Tuesday
16.50 - 17.50
Nivo Noord zalen
The formation of acid mine drainage (AMD) implies the weathering and oxidation of the iron sulphide
minerals present in mining areas and the formation of large amounts of secondary iron precipitates. The
presence of these secondary iron precipitates can be considered of great importance, since they are naturally occurring scavengers for most of the contaminants that acumulate in these areas and their presence
controls its mobility and availability. Since sorption is one of the best methods for the removal of contaminants, natural aluminium and iron oxides from AMD are the main responsibles for the speciation and fate
of heavy metals and other species commonly found in mining areas to prevent its leaching through the soil
profile and the contamination of ground and surface waters.
In the present study we have precipitated iron oxides from water samples collected at two different points
of the Touro abandoned copper mine (Iberian Piritic Belt, Galicia, NW Spain). The precipitates were characterized and the XRD and SEM images showed that they looked very much like schwertmannite. The
retention of Cu, Cd, Ni and Pb on these AMD precipitates was analyzed under different experimental conditions (different pH) and the affinity series found was: Cu > Pb > Ni > Cd (see figure).
Also, the ageing of the precipitates was conducted during 1 and 6 months at the original pH of the AMD
water samples (pH ~ 3). It was found that depending on the origin of the sample and the ageing time, the
precipitate can undergo a transformation from an amorphous swertmannite–like form to a crystalline
goethite–like form. The different retention of the same heavy metals previously studied cofirmed the
transformation process sufered by the iron oxides. In an attempt to model heavy metals retention in these
natural iron oxides analogous to some sinthetic oxides, surface complexation models have been applied.
94
Adsorption and aerobic biodegradation of three selected endocrine disrupting
chemicals in artificial groundwater recharge with treated reclaimed municipal
wastewater through river utilization
Weifang Ma a*, Bin Chenb, Xiang Cheng a, Fangang Zengb, Chao Niea, Fangfang Sua
a College of Environmental Science and Engineering, Beijing Forestry University, Beijing 100083, China
b School of Environment and Natural Resource, Renmin University of China, Beijing 100872, China
*Corresponding author: Tel.:+86 10 62336615; E-mail: [email protected]
16.50 - 17.50
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95
Tuesday
EDCs (endocrine disrupting chemicals) pollution in river-based artificial groundwater recharge using reclaimed municipal wastewater poses a potential threat to groundwater drinking water supplies in Beijing, China. Laboratory leaching column experiments simulating recharge were conducted to study adsorption, aerobic biodegradation, transport and leaching characteristics of three selected EDCs 17β-estradiolum(E2),
ethinylestradiol(EE2) and bisphenol A(BPA). Representative soil vadose zone media from the ChaoBai River
were used as filler for the three columns. The three columns were operated in the condition of continual
sterilization recharge, continual recharge and wetting and drying alternative recharge. The results showed
that the attenuation of EDCs was in the order of E2 > EE2 > BPA, which followed the principle of first-order
kinetics. The EDCs decay rate constants were 5.6 m-1, 5.2 m-1 and 4.7 m-1 for E2, EE2 and BPA in continual
recharge system, respectively. The adsorption ratios of the soil were 98%, 96% and 92%. While, the biodegradation ratios were 1.1%, 1.7% and 4.2%. The EDCs decay mainly depended on soil adsorption with
depth. The EDCs attenuation by unit mass was 1.685mg (100g)-1, 1.032 mg (100g)-1and 0.172 mg (100g)-1,
respectively. The inflection points of EDCs concentration at different depths were 0.3m. In one column
system with wetting and drying alternative, the concentrations of EDCs dropped 0.2%, 1.2% and 2.3%
than the continual recharge system. The EDCs biodegradation was affected by water temperature; when
the temperature was below 5 °C, the conversion of EDCs did not change significantly with depth and time.
The adsorption capacity decreased 8%, 7% and 13% when the temperature increased from 20 °C to 40 °C.
Groundwater EDCs pollution was related to the adsorption and degradation capacity of the soil vadose
zone media. To avoid or minimize possible EDCs contamination of groundwater in artificial groundwater
recharge areas, the amount of EDCs in treated reclaimed municipal wastewater has to be determined
and minimized by optimizing reclaimed water treatments, optimizing the management of the recharging
operation and enhancing the ecological purification function of rivers.
Study of Electrosorption Performance of Nanostructured Carbon Electrodes in
Capacitive Deionization
Chia-Hung Hou*, Chen-Shiuan Fan, and Nei-Ling Liu
Graduate Institute of Environmental Engineering, National Taiwan University, Taiwan
Tuesday
16.50 - 17.50
Bentacera zaal
(E-mail: [email protected])
Capacitive deionization (CDI), or referred to as electrosorption process, is a promising nanotechnology as
a means of saving energy and producing purified water. The working principle of CDI relies on electrochemical separation of ions onto highly porous carbons, which is similar to that of energy storage in supercapacitors. It is noted that the choice of nanostructured carbon electrodes is the key factor to determine
the deionization performance. The objective of this study is to identify the effect of pore characteristics
on desalting capability in the CDI process. Several carbon materials with various porosities, such as carbon
aerogel, activated carbon, multiwalled activated carbon, and ordered mesoporous carbon, are tested.
The capacitive behaviors of carbon electrodes are evaluated by using cyclic voltammetry. Electrosorption
experiments with a CDI cell are carried out to assess the deionization performance of carbon electrodes.
The obtained results show clear trends in the relationship between the electric double-layer capacitance
and electrosorption capacity. Also, the carbon materials possessing the different pore sizes show different
types of cyclic voltammograms. One can see that the electrosorption capacity strongly depends on the
specific surface area and the pore size distribution of carbon materials themselves. The carbon electrodes
associated with larger mesoporosity result in a higher effective surface area and greater electrosorption
capacity. The good electrosorption performance could be attributed to the presence of mesopores that
are less affected by double-layer overlapping and then facilitate ion transport in the CDI process. More
specifically, Grand Monte Carlo simulations (GCMC) can be further used to provide the insights into ion
distribution inside charged nanopores and to predict its electrosorption capacity. The findings of this work
can provide useful information to search the desirable carbon materials in CDI process.
96
Pore-structure of Activated Carbon Fibers on Capacitive Deionization
Jiyoung Kim1,2, Dong-Hyun Peck2, Byungrok Lee2, Seong-Ho Yoon3, Doo-Hwan Jung1,2,*
Advanced Energy Technology, University of Science and Technology (UST), 113 Gwahangno, Yuseong--gu, Daejeon 305-333, Korea
1
Hydrogen and Fuel Cell Department, Korea Institute of Energy Research (KIER), 102 Gajeong-ro, Yuseong-gu, Daejeon 305-343, Korea
2
Institute for Materials Chemistry and Engineering, Kyushu University, 6-1 Kasuga-koen, Kasuka, Fukuoka, 816-8580, Japan
3
* E-mail: [email protected]
We develop the capacitive deionization (CDI) system for the purification of sodium-chloride containing
water using activated carbon fibers. The pitch-based activated carbon fibers (OG-series; 7A, 10A, 15A,
20A from Osaka gas Co. Ltd. Japan) have varying degree of activation with different surface area and pore-distribution. These materials were applied in CDI system and evaluated the ion adsorption capacity of
sodium/chloride respectively. The experiments were conducted at various applied voltage, solution feed
rate, and concentration. The results of experiments indicate that the pore structure of OG-7A is suitable
for sodium ion adsorption and OG-10A or OG-15A has adequate pores for chloride. The detailed relations
between the desalination of sodium/chloride ions and pore-structure of activated carbon fiber are discussed in this presentation.
Tuesday
16.50 - 17.50
Bentacera zaal
97
Capacitive Deionization with PZC-Modified Carbon Xerogel: Half-Cell and System
Analysis for Long-Term Operation
James Landon, Xin Gao, Ayokunle Omosebi, Kunlei Liu
2540 Research Park Drive, Center for Applied Energy Research, University of Kentucky, USA
[email protected] www.caer.uky.edu
Tuesday
16.50 - 17.50
Bentacera zaal
Capacitive deionization (CDI) is an emerging water treatment technology that holds many benefits over
existing pressurized membrane separation systems including low energy cost of separation, modular design, and possibly lower capital and maintenance costs.(1) This growing technology has not become commercially widespread for a few reasons:
1 Cost competitive carbon electrodes capable of higher salt capacities are still needed
2 Demonstration of longer equipment lifetime needs to be accomplished
3 Energy benefits of the operation need to be further shown and compared to existing reverse osmosis
(RO) systems and other combined water treatment technologies
4 Marketing the technology needs to take place to interested customers in a variety of markets
In recent years, CDI has come a long way towards meeting these goals, especially with the inclusion of
membranes which are capable of not only increasing the salt capacity of the electrodes, but also of enabling fast regeneration of the adsorption surface.(2, 3) While the addition of membranes is quite attractive, it comes at the cost of added complexity and the increased possibility for fouling.
An alternative to membrane capacitive deionization (MCDI) is the use of a potential of zero charge (PZC)
modified carbon electrode that can increase the salt capacity of the electrode while also possibly decreasing the overall costs of the device.(4-6) These cost effective PZC-modified carbons can increase charge
efficiencies by up to 50%.(7) However, the functional groups on the carbon surface will change over time
as Faradaic oxidation reactions occur. These new oxide groups can substantially affect the salt capacity
of the carbon electrodes and must be dealt with to maintain the separation ability of the CDI process. In
the work presented here, various mitigation mechanisms will be shown that can extend the lifetime of a
CDI cell by controlling the surface oxide groups and limiting the shifting of the PZC into regions that can
negatively affect the electrosorption capacity and charge efficiency. Both chemical and electrochemical
options will be demonstrated with cycling experiments carried out at greater than 150 cycles.
References
1. M. A. Anderson, A. L. Cudero and J. Palma, Electrochimica Acta, 55, 3845 (2010).
2. P
. M. Biesheuvel and A. van der Wal, Journal of Membrane Science, 346, 256 (2010).
3. R
. Zhao, P. M. Biesheuvel and A. van der Wal, Energy & Environmental Science, 5, 9520 (2012).
4. E . Avraham, M. Noked, I. Cohen, A. Soffer and D. Aurbach, Journal of The Electrochemical Society, 158, P168 (2011).
5. X
. Gao, J. Landon, J. K. Neathery and K. Liu, Journal of The Electrochemical Society, 160, E106 (2013).
6. J . Landon, X. Gao, B. Kulengowski, J. K. Neathery and K. Liu, Journal of The Electrochemical Society, 159, A1861 (2012).
7. X
. Gao, A. Omosebi, J. Landon and K. Liu, Electrochemistry Communications, 39, 22 (2014).
98
Oral presentations Wednesday
99
DIFFUSION OF ANTHROPOGENIC ORGANIC MATTER IN CLAY ROCK
R. Dagnelie, J. Radwan, P. Nerfie
CEA, DEN, DPC, SECR, Laboratory of Radionuclide Migration Measurements and Modelling, F-91191 Gif-sur-Yvette, France. Corres-
Wednesday
9.20 - 10.40
Rabobank zaal
ponding author: [email protected]
Small organic molecules are present in natural soils, sedimentary rocks, but also in mixed radioactive or
hazardous wastes. Some organics are released by wastes and these co-contaminants potentially affect the
migration of cations. The sorption of organic compounds in soils is largely studied [1], but the quantification of organics diffusion parameters is less common because of time consuming experiments. In this work,
we focused on transfer parameters in clayrock of anthropogenic organics which are found to be relevant in
the field of radionuclide migration. Results are discussed with emphasis on diffusive behaviour and effects
on cations and complexes mobility. The Callovo-Oxfordian clayrock (COx) is investigated by the French
radioactive waste management agency (ANDRA) in the context of the underground retrievable nuclear
waste repository project (Cigéo). There is already a large dataset on ions diffusion in COx clayrock [2,3].
Recent results obtained on isosaccharinate, EDTA, oxalate and phthalate will be presented. The sorption
isotherms, hysteresis and diffusion parameters have been quantified using 14C-radiolabelled tracers. The
effective diffusion coefficient, De, of organic species is mainly driven by anionic exclusion and size effects,
whereas diffusion of cations is mostly affected by hydration and surface effects (Figure 1). Diffusion experiments still confirmed a low sorption of organics on clayrock.
In a second part, we focused on europium sorption in presence of organic molecules. The sorption of
europium at low organic concentration is reversible and almost independent of the presence of ligands. A
decrease of europium sorption appears with the formation of anionic complexes. At high concentration of
organics, the solid/solution distribution ratio, Rd(Eu), reaches a plateau and displays a strong hysteresis.
This result may indicate a sorption mechanism with ligands acting as a bridge between mineral surfaces
and europium and possibly a modification of the sorbing phase. Other experiments are necessary to confirm these hypotheses and to determine which solid phases are involved. The characterization of such
a behaviour was useful for assessing the relevant species, concentrations and effects of anthropogenic
organic in the field of deep geological nuclear waste storage.
References
1. Pignatello, J. J. (2000) The measurement and interpretation of sorption and desorption rates for organic compounds in soil media. Advances in Agronomy, 69, 1-73.
2. Melkior, T. et al. (2007) Diffusion coefficients of alkaline cations in Bure mudrock. Physics and Chemistry of the Earth, Parts A/
B/C, 32, 453-462.
3. Descostes, M., et al. (2008) Diffusion of anionic species in Callovo-Oxfordian argillites and Oxfordian limestones (Meuse/Haute-Marne, France). Applied Geochemistry, 23, 655-677.
4. Dagnelie, R. et al. (2014) Sorption and diffusion of organic acids through clayrock: comparison with inorganic anions (not published, article submitted).
This work was partially financed by the ANDRA.
Figure 1. Diffusivity in COx clayrock : ∏=[De/De(HTO)]/[D0/D0(HTO)].
Values for alkaline cations (Top, [2]) and various anions (Bottom,
[3,4]).
100
Uranium migration at nuclear waste management facilities: experimental versus
thermodynamic modeling
Olga L. Gaskova, Boguslavsky Anatoly E., Shemelina Olga V.
Institute of Geology and Mineralogy, SB RAS, Novosibirsk; Novosibirsk state University, Russia
[email protected]
Uranium is a common aquifer contaminant of concern at nuclear waste management facilities around the
world. The most significant pathway for uranium migration is via groundwater transported away from such
sites. Uranium mobility in oxic groundwater is believed to be controlled by adsorption of U(VI) on mineral
surfaces of iron oxides and clay minerals due to their high sorptive capacities and common occurrence.
Liquid radioactive wastes of the Angarsk Electrolysis Chemical Complex AEC (Irkutsk region, Russia) and of
the Electrochemical Plant ECP (Zelenogorsk, Krasnoyarsk region, Russia), which have produced enriched
uranium since 1960s, are formed during neutralization of nitric slurry after the U extraction by hydrated
lime. A significant part of the residual U precipitates as poorly soluble calcium uranates or during the
crystallization of calcite and other Ca-phases in the sludge ponds. One of the outstanding tasks in the study
of (co)precipitation is the investigation of pH effect and carbonation of those waste disposal systems, in
which high pH-values are established. The results of detailed sampling of groundwater and surface water
near the storage sites of radioactive waste are presented elsewhere (Gaskova, Boguslavsky, 2013). The
purpose of this investigation is to describe the results of dynamic experiments of the waste materials leaching by artificial groundwater and of the U sorption with two types of clay wall-rock sample as a function
of rock:water ratio. Different thermodynamic models have been employed to elucidate uranyl sorption
onto Fe-oxides, clay and carbonate minerals to explain the mechanisms controlling the uranium uptake.
Thermodynamic modeling at 25°C and 1 bar total pressure was performed with the “HCh” code using a
free energy minimization algorithm (Shvarov, 2008). We modeled the heterophase 13-component system
H-O-Ca-Si-Al-Fe-Mg-K-S-N-C-F-U system; the solid, dissolved and adsorbed U-species were incorporated
into the model using data from the literature. Table 1 and Fig. 1 is an example of interrelated experimental
and thermodynamic modeling results.
Table 1. Mineral composition, conditions and results of dynamic experiments during 80 days
Zelenogorsk ECP waste
CaF2, CaSO4*2H2O, Mg(OH)2, CaCO3, trace of Quartz, CaCO3, CaSO4*2H2O, Ettringite, minor Quartz (5-10%),
CaAl2(CO3)2(OH)4*6H2O, Ettringite, Voltaite, Fe- and Fe (hydro)oxides, CaF2, trace of NaAl(SO4)2*12H2O,
Al-oxides, Illite-smectite. Micron-sized isolation of CaSO4*0.5H2O, Ca2(CO3)SO44H2O and Chlorite. U-minerU-Ca-phases. Total U content is ~0.2%.
als were not detected. Total U content is ~0.01%.
Wednesday
Angarsk ECC waste
Weight leaching of solid sample (%), mineralization of solution (mSm/cm) and final U concentration (mg/L)
39%, 1.8 – 0.4 mSm/cm, nearly constant 0.002 mg/L
9.20 - 10.40
Rabobank zaal
6%, 0.35 mSm/cm, nearly constant 0.23 mg/L
The percentage of solid U extracted by the CH3COONH4 + HNO3 solution (connected in the carbonate fraction)
82%
93%
101
S O4
2
80%
G yps um
C hlorite
60%
E ttringite
0
2-
C alcite
40%
30%
20%
F luorite
AlOOH
0%
10,71 10,46 10,22 10,00 9,47
8,49
8,28
8,08
7,93
-4
-5
-4
-6
Utota l
C O2
-8
-10
8,97
-3
-2
-6
10%
6,36
-1
-2
0
logCi, mg/L
70%
50%
C a tota l
4
F eOOH
90%
-7
-8
-9
-10
10,7 10,5 10,2 10,0 9,5 9,0 8,5 8,3 8,1 7,9 6,4 pH
Fig. 1. Modeling data for U-containing sludge dissolution showing both (left) percentage of minerals and (right)
solution composition versus pH at different pCO2,atm.
References
1. Gaskova O., Boguslavsky A. Groundwater geochemistry near the storage sites of low-level radioactive waste: Implications for
uranium migration. Procedia Earth and Planetary Science, 2013 V.7. p. 288-291.
2. Shvarov Yu.V. HCh: New potentialities for the thermodynamic simulation of geochemical systems offered by Windows // Geochemical International 2008; 46: 834-839.
Acknowledgements
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This work was supported by the Russian Fund for Basic Research (project number is 13-05-00032).
102
logCO 2,atm
NaC a 2Al5S i5O 20*6H 2O
100%
Adsorption of sodium dodecylbenzene sulfonate in highly humic volcanic ash soil
Farook Ahmed1, Munehide Ishiguro2*
1 Graduate school of Environmental Science, Okayama University,
3-1-1 Tsushima-naka, Okayama 700-8530 Japan
2Laboratory of Soil Conservation, Research Faculty of Agriculture, Hokkaido University, Sapporo, 060-8589 Japan
*[email protected]
Sodium dodecylbenzene sulfonate (DBS) is a very useful and widely used anionic surfactant. This surfactant sometimes creates environmental problems when it is released into the environment. However, the
factors influencing the adsorption of DBS in soil have not been studied well. In this study, the influence
of the potential at the adsorption site on the adsorption of DBS in a soil was first elucidated by using a
theoretical adsorption equation. The soil was a highly humic soil with a negative charge. The amount of
DBS adsorbed was measured with a batch method for different electrolyte concentrations of NaCl at pH
4.5 and 6.5. The adsorption site potential of the soil was obtained with the modified Langmuir adsorption
equation. The adsorption of DBS decreased as the electrolyte concentration decreased and as the pH increased because the repulsive electric potential between DBS and the soil increased. These results were
confirmed by the obtained adsorption site potential and the measured zeta potential. The difference between the adsorption of DBS with a linear and with a branched carbon chain was also detected, and this
difference was related to the free energy of micellization. Because DBS adsorption is strongly affected by
electrolyte concentration and pH, these two factors must be carefully considered to predict the fate of DBS
in environmental applications.
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Fig. 1 Influence of electrolyte concentration and adsorption site potential on DBS adsorption isotherm.
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103
Coupled Effects of Hydrodynamic and Solution Chemistry Conditions on Long-Term
Nanoparticle Transport and Deposition in Saturated Porous Media
Salini Sasidharan1, 2, Saeed Torkzaban1, Scott A. Bradford3
1CSIRO Land and Water, Glen Osmond, SA 5064, Australia
2National Centre for Groundwater Research and Training, Flinders University, Adelaide, SA 5001
3USDA, ARS, Salinity Laboratory, Riverside, CA 92507
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This study aims to systematically explore the coupled effects of hydrodynamic and solution chemistry
conditions on the long-term transport and deposition kinetics of nanoparticles (NPs) in saturated porous
media. Column transport experiments were carried out at various solution ionic strengths (IS), ion types
(monovalent and divalent), and flow velocities utilizing negatively charged carboxyl-modified latex NPs
of two different sizes (50 and 100 nm) using acid washed medium sized river sand. Most experimental
studies of NP deposition in porous media have focused on the initial clean bed deposition. In this study
the experiments were designed to obtain the long-term breakthrough curves (BTCs) in order to unambiguously determine the full deposition kinetics and the fraction of the solid surface area (Sf) that was
available for NP deposition. The experimental evidence accessible in the literature on the dependency of
Sf on physiochemical and hydrodynamics factors, especially for NP are very narrow. The BTCs exhibited a
bimodal shape with increasing solution IS; e.g., BTCs were initially delayed, then they rapidly increased,
and then slowly approached the influent particle concentration. Most research were conducted in the
presence of monovalent electrolyte. In this study we compared the effect of monovalent (NaCl) and divalent (CaCl2) solution chemistry. NP deposition was much more prominent in the presence of Ca2+ than Na+
at any given solution IS. Deposition dynamics of NPs was successfully simulated using a two-site kinetic
model that accounted for irreversible deposition and blocking (e.g., a decreasing deposition rate as the
available site filled) on each site. Results showed that Sf values were controlled by the coupled effects of
flow velocity, solution chemistry, and particle size. Data analyses further demonstrated that only a small
fraction of solid surface area contributed in NP deposition even at the highest IS (60 mM NaCl and 3mM
CaCl2) and lowest flow velocity (1 m/day) tested. Consistent with previous studies conducted with clean
sand, our results imply that NP deposition occurred because of physicochemical interactions between the
negatively charged COOH groups on the NPs and nanoscale physical and/or chemical heterogeneities on
the sand surfaces that produced localized nanoscale favorable sites. Furthermore, our results suggest that
the NP interactions with the collector surfaces tended to strengthen with increasing contact time.
104
Coverage and disruption of phospholipid membranes by oxide nanoparticles
Harke Pera, Tom Nolte, Frans Leermakers, Mieke Kleijn
Laboratory of Physical Chemistry and Colloid Science, Wageningen University, The Netherlands
e-mail [email protected], website www.wageningenur.nl/pcc
References
1. H. Pera, J.M. Kleijn, F.A.M. Leermakers, “Interaction of Silica Nanoparticles with Phospholipid Membranes”, Chem. Lett. 41
Wednesday
The interaction between nanoparticles and biological membranes has been subject of much research over
the past decades, mainly for two reasons. On the one hand, engineered nanoparticles are used in many
products, for example cosmetics, tires, coatings and anti-bacterial substances. Since a large part of these
particles ends up in the environment, concerns have raised with respect to their possible (cyto)toxicity.
On the other hand, nanoparticles may be used as vehicles for drug delivery into cells. In both cases an important question is whether they can enter a living cell, i.e., how do they interact with the cell membrane
and can they cross it?
In our studies we focus on the interaction of oxide nanoparticles, in particular silica and titanium dioxide
with phospholipid membranes. We show how electrostatics plays an important role in this interaction. For
this we systematically varied the charge density of both the lipid membranes by changing their composition, and the oxide particles by changing the pH. Results from our fluorescence vesicle leakage assay [1]
are combined with recent data on particle adsorption onto supported lipid bilayers obtained by optical
reflectometry and AFM imaging. Self-consistent field (SCF) modelling [2] has been applied to interpret the
results on a molecular level.
At low particle charge density no barrier for adsorption exists and the adsorption rate is determined by
transport kinetics only. Both the adsorption rate and adsorbed amounts drop with increasing (negative)
charge densities on particles and membranes (see e.g. Figure 1) due to electric double layer repulsion. This
is confirmed by the effect of the ionic strength. SCF calculations show that charged nanoparticles change
the structure and dynamics of lipid bilayers by a reorientation of the zwitterionic phosphatidylcholine
(PC) head groups. This explains the affinity of the silica particles for PC lipid layers, even at relatively high
particle charge densities.
Particle adsorption does not always lead to disruption of the membrane integrity as is clear from comparison of the leakage and adsorption data. Using AFM we can distinguish between particles that penetrated
into the bilayer and particles that resided on top of the bilayer, depending on physicochemical conditions.
Our results may be extrapolated to a broader range of oxide nanoparticles and ultimately be used for establishing more accurate nanoparticle toxicity assessments.
(2012) 1322 - 1324.
2. H. Pera, J.M. Kleijn, F.A.M. Leermakers, “Linking lipid architecture to bilayer structure and mechanics using self-consistent field
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modelling”, J. Chem. Phys. 2014, accepted.
Figure 1. Adsorbed amounts of silica particles on sup- Figure 2. AFM images of silica particles (diameter 15 nm)
ported lipid membranes as a function of particle char- on uncharged DOPC membranes adsorbed at pH 10.6
ge density. The (negative) charge on the membranes (left) and pH 6.0 (right). The particle charge densities were
increases with DOPG (a negatively charge phospholi- around –0.33 C/m2 and –0.01 C/m2, respectively.
pid) content.
105
Shape evolution synthesis of crystalline hematite (α-Fe2O3) nanoparticles using ascorbic
acid and tartaric acid
Wen-Feng Tan*, †, Ya-Ting Yu†, Zhen-xin Tao †, Ming-Xia Wang †, and Luuk K. Koopal ‡
† College of Resources and Environment, Huazhong Agricultural University, Wuhan, P. R. China.
‡ Laboratory of Physical Chemistry and Colloid Science, Wageningen University, Dreijenplein 6, 6703 HB Wageningen, the Netherlands
Iron oxides and hydroxides are widely present in nature and nano-particles of iron minerals are distributed throughout the atmosphere, oceans, groundwater, surface waters, soils, in and/or on most living
organisms. The formation of hematite can be promoted by employing Fe(II). However, Fe(II) is an unstable
reductant that can be oxidized easily when exposed to air. Organic ligands where Fe(II) is produced in the
reaction mixture instead of added could avoid this disadvantage. These ligands adsorb to the ferrihydrite
and serve as electron channel during the reduction of Fe(III) of ferrihydrite to Fe(II). Ascorbic acid (AA) and
tartaric acid, which are widely present in nature, are good candidates for the reduction of Fe(III) to Fe(II)
as electron donor.
Ascorbic acid instead of Fe(II) effectively catalyzes the formation of α-Fe2O3 and the particle morphologies
are successfully controlled by the amount of ascorbic acid for the first time. Spherical, ellipsoidal and elongated hematite particles have been obtained (Fig. 1). Various shapes of the prepared α-Fe2O3 on catalyzed
degradation of methylene blue are substantially different. The elongated particles that had the highest
specific surface area were most effective.
Tartaric acid as both a reducing agent and a template also control particle size and morphology of hematite. The initial pH was a crucial factor to control morphology of hematite. The products were corn-like at
initial pH 7 through oriented attachment (Fig. 2), but changed to be round by ostwald ripening mechanism
at high pH (pH=11).
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Fig. 1 Schematic illustration of the shape development
of hematite synthesized at different AA/Fe(III) ratios
106
Fig. 2 SEM images of hematite synthetized at pH 7
Removal of organic pollutants from water by TiO2/CnTAB Nanoskeleton
Toshio Sakai*
Department of Chemistry and Material Engineering, Faculty of Engineering,
Shinshu University,
4-17-1 Wakasato, Nagano 380-8553, Japan
Email: [email protected],
URL:http://www.shinshu-u.ac.jp/faculty/engineering/chair/chem005/Index_Eng.htm
Adsorption is considered as one of the effective and versatile methods for removal of the chemical contaminants from wastewater. Thus, the development of absorbents is an important and challenging task
for environmental remediation. In recent years, the combination of titanium dioxide (TiO2) with organic/
inorganic hybrid porous materials such as organic molecules-grafted mesoporous materials and surfactant-templated mesoporous materials have attracted attention because organic domains in the mesoporous inorganic materials interact with organic pollutants and TiO2 degrades the organic pollutants adsorbed on the mesoporous materials due to the photocatalysis. Then, in this work, we develop the hybrid
particles of TiO2 and surfactant, and examine the potential of the hybrid particles as both adsorbent and
photocatalyst for removal of organic pollutants from water. The hybrid particles (named as TiO2/CnTAB
Nanoskeleton) was prepared through the so-gel reaction of titanium oxysulfate sulfuric acid hydrate (TiOSO4·xH2SO4·xH2O) initiated by alkyltrimethylammonium bromide (CnH2n+1N(CH3)3Br, CnTAB; n = 12, 14, 16
and 18) micelles in an aqueous solution at 60 ˚C for 24 h. The TiO2/CnTAB Nanoskeleton is a hexagonal-structured assembly of nanocrystalline anatase TiO2 and CnTAB. We found that alkylphenols dissolved
in water were removed through the adsorption of alkylphenols onto TiO2/CnTAB Nanoskeleton. On the
other hand, no significant adsorption of alkylphenols onto TiO2 Nanoskeleton (that was obtained after
calcination of TiO2/CnTAB Nanoskeleton) was observed. This indicates that the adsorption of alkylphenols
onto the TiO2/CnTAB Nanoskeleton is attributed to the hydrophobic interaction between alkylphenols and
CnTAB domains. We also found that alkylphenols dissolved in water was completely removed by the combination of adsorption and photocatalysis of TiO2/CnTAB Nanoskeleton under UV irradiation. This proves
that the TiO2/CnTAB Nanoskeleton acts as in tandem an adsorbent and a photocatalyst for removal of
organic pollutants dissolved in water.
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107
Smart Hybrid Nano-Composite Devices for Removal of PAH Micro-pollutant from
Wastewaters
Nadine Bou Orm, Stéphane Daniele*
University Lyon 1, Institute of Research of Catalysis and Environment of Lyon, UMR-CNRS 5256, 2 avenue Albert Einstein, 69626 Vil-
Natural and drinking water supplies are being increasingly contaminated with emerging organic micro(diluted-) pollutants such as Polycyclic Aromatic Hydrocarbons (PAHs), which have been identified as carcinogenic and are non-degradable. Absorption is considered to be a very effective method of quick lowering
of the concentration of dissolved pollutant in an effluent. However, traditional treatment using membrane
or activated carbons have some limitations such as fouling and weak sorption ability due to their weak
interaction with the target contaminants or difficulties to be regenerated respectively and, hence, require
a radical change in the fundamental structure of the substrates.
This presentation will address a new concept in efficient nano-sorbent for the sustainable removals of PAH
micro-pollutant from wastewaters. The technology is based on the conception of novel nano-composite
materials consisting of technical textile fibers functionalized by Organic/Inorganic nano-coatings (see figure below). We will discuss results from synthesis and characterizations of new molecular precursors for the
Sol-Gel process to the remarkable advantages of the resultant hierarchical micro-, nano-structured nanocomposites, giving low cost and strong mechanical structures that can withstand high water flow rate for
long time (a prerequisite. We will also demonstrate the relationships between the mode of coordination,
the nature of the trapping sites of the ligand (pi-stacking) and high removal capacities and selectivities,
fast adsorption rates and recycling properties for PAH organic moieties.
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leurbanne cedex, France ; email : [email protected]
108
Temperature effects on the desalination of water
Mathijs Janssen, Andreas Härtel, and René van Roij
Institute for Theoretical Physics, Utrecht University, Leuvenlaan 4, MG 305, 3584 CE Utrecht, The Netherlands
phone: +31 30 253 2955
mail: [email protected], [email protected], [email protected]
Where rivers flow into the sea, an enormous amount of energy (about 2kJ/L, equivalent to a 200m waterfall) is dissipated, due to irreversible mixing of fresh and salty water. This energy is extracted in a blue
engine by selectively intercepting some of the involved ions during this process. While older devices rely
on membranes, which are prone to fouling, a new device has been proposed by Brogioli [1], which acts by
cyclic charging and discharging of porous electrodes immersed in sea and river water. The reverse process
is desalination, which produces fresh water at the expense of energy input.
We study both processes within the framework of modified Poisson Boltzmann theory and Density Functional Theory. Our theories include packing effects, which become important in the nanometer scale pores
of the electrode material.
We investigated the effect that varying the temperature of the water has on the properties of blue engine
and desalination cycles. Desalination cycles were found to be most effective when cold water is used. There is a ~10% decrease in required energy when changing from equatorial to arctic sea water.
Furthermore, we studied the effect of using water at different temperatures within one cycle. Saline water
reservoirs at different temperatures can be obtained by e.g. pumping sea water from depths to the surface
or by using cooling water from industrial facilities in an intelligent way. Desalination becomes increasingly
cheap when performing the charging step in sea water of lower temperature than the discharging step.
Interestingly, the characteristics of the engine (pore size, pore volume, bath volume) can be tailored such
that the required energy vanishes already for small temperature differences.
These positive temperature effects on the efficiency are not at all exclusive to desalination cycles, similar
temperature effects are also observed in blue energy cycles. We find that blue energy harvesting can be
enhanced when fresh water is used which has a higher temperature than the sea water. For large temperature differences of the order of 50 degrees this boosts the work per cycle by a factor of two, compared
to existing techniques (see figure).
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References
1. D. Brogioli, Phys. Rev. Lett. 103, 058501 (2009)
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Figure: Blue energy cycle in the potential – charge representation. Stroked lines represent the upper part of the cycle, connected to fresh water reservoirs of different temperature.
109
Structural and size effects on the desalination cycle of water
Andreas Härtel, Mathijs Janssen, and René van Roij
Institute for Theoretical Physics, Utrecht University, Leuvenlaan 4, MG 305, 3584 CE Utrecht, The Netherlands
phone: +31 30 253 2322
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We investigate the effect, which varying pore and engine sizes have on the properties of the desalination
cycle. To obtain comparative results, we introduce the size ratio x=Vb/(Vb+Ve) between the volume Ve of
the capacitive engine and Vb of the bath, which is desalinated. By this, we compare desalination cycles,
which are obtained by using electrodes, completely build of pores with a certain fixed size. We find that
the size ratio x does effect the amount of energy that is needed to desalinate one liter of water; interestingly, the desalination cycle becomes optimal for very large ratios x, when the desalination bath becomes
very large in comparison to the engine (see figure). Thereby, the required energy can vary by more than
15 percent.
Furthermore, the optimal pore size also depends on the size ratio x. We discuss this behavior and physical
as well as economical limits of this optimization. Finally, our findings can easily be mapped onto the inverse cycle, a blue engine, which allows a maximization of the harvested blue energy.
References
D. Brogioli, Phys. Rev. Lett. 103, 058501 (2009)
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1
Figure: Required energy for the desalination of one liter of sea water, shown
against the ratio x=Vb/(Ve+Vb) for fixed pore sizes L.
110
Membrane Capacitive Deionization: definitions and double layer modeling
P.M. Biesheuvel1,2, R. Zhao1,2, S. Porada2, H.H.M. Rijnaarts1 and A. van der Wal1,2
Department of Environmental Technology, Wageningen University, Bornse Weilanden 9, 6708 WG Wageningen, The Netherlands.
1
Wetsus, centre of excellence for sustainable water technology, Oostergoweg 7, 8911 MA Leeuwarden, The Netherlands
2
Membrane Capacitive Deionization (MCDI) employs ion-exchange membranes together with porous carbon electrodes to desalinate water. In MCDI ions are stored both in the interparticle pore space between
carbon particles, as well as within the electrical double layers (EDL) formed inside the carbon micropores.
In the micropore EDLs, electronic charge in the carbon is exactly matched by the ionic charge in the water-filled micropores (diffuse or Donnan layer), see Fig. 1. The main advantage of MCDI is that the charge
efficiency is much higher than in CDI, at low enough salt concentration approaching unity. This leads to
a reduction in energy consumption. Also, in MCDI a reversal of the voltage is possible during discharge
(regeneration), which helps to speed up ion release. In CDI, voltage reversal lead to a frequency doubling
of the CDI cycles. Finally, in MCDI it works better than in CDI to operate in constant-current mode, leading
to a stable effluent salt concentration at a level that can be tuned by modifying the current.
In the presentation we discuss different meanings of terminology used in the CDI-field for efficiency:
charge efficiency, current efficiency, Coulombic efficiency, and salt removal efficiency. We compare electrostatic double layer models that can be used to describe ion adsorption and charge (Gouy-ChapmanStern versus modified-Donnan model). Finally, we describe how these microscopic EDL-models can be
included in a two-dimensional electrode transport model.
A
"B"
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References
1. R. Zhao, P.M. Biesheuvel and A. van der Wal, “Energy Consumption and Constant Current Operation in Membrane Capacitive
Deionization,” Energy & Environmental Science 5 9520-9527 (2012).
2. R. Zhao, M. van Soestbergen, H.H.M. Rijnaarts, A. van der Wal, M.Z. Bazant and P.M. Biesheuvel, “Time-dependent ion selectivity
in capacitive charging of porous electrodes,” J. Colloid Interface Sci. 384 38-44 (2012).
3. P.M. Biesheuvel, S. Porada, M. Levi, M.Z. Bazant, “Attractive forces in microporous carbon electrodes for capacitive deionization,”
J. Solid State Electrochem. (2014). http://dx.doi.org/10.1007/s10008-014-2383-5
111
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Fig. 1. Classical Gouy-Chapman-Stern EDL model vs modified-Donnan model for carbon micropores.
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Carbon matrix
Carbon matrix
St St
Multiphysics simulation of Membrane Capacitive Deionization for mixed streams
Dennis Cardoen1,2, Bruno Bastos Sales1, Joost Helsen1, Arne Verliefde2
1
VITO NV, Separation and Conversion Technology unit, Boeretang 200, 2400 Mol, Belgium
2
Universiteit Gent, Particle and Interfacial Technology group, Coupure Links 653, 9000 Gent, Belgium
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[email protected] / www.vito.be
Membrane capacitive deionization (MCDI) has emerged over the past years as an energy- and cost-efficient technology for desalination of waters with low to moderate salt content in applications such as
domestic water softening or desalination of cooling tower make-up water [1]. With the aim of broadening
the range of applications of this technology, we have been investigating the possibility of MCDI treatment
for more ‘complex’ wastewaters and industrial process streams - such as biomass hydrolysates [2] - which
contain both salts and organic compounds. This combination tends to be problematic for conventional
separation processes; therefore there is a need for new techniques for efficient recovery of the target
compounds and/or water. The low fouling susceptibility and high energy efficiency of MCDI make it a potential alternative separation technology for such types of streams. Initial tests indicated that the current
commercial MCDI setups do not always operate optimally in the presence of organic compounds. Therefore a better understanding of the behavior of different types of organics within MCDI, and of the key
factors determining overall performance on mixed streams is needed, in order to develop tailored designs
and operational modes.
In the coming future, the goal of this research is to develop a COMSOL multiphysics FEM model to develop
insight into the transport processes occurring in MCDI applied to mixed streams, and subsequently use
this model as a design aid for novel applications.
Points of attention are CFD-based geometry optimizations to minimize dispersion (in order to e.g. enhance product recovery), strategies for mitigating concentration polarization effects on both the spacer
and electrode side of the membrane, prevention of faradaic reactions, fouling, scaling and clogging, and
selection of ion exchange membranes with an optimal balance between mobility of organics and electrical
resistance.
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References
1. Celine Huyskens, Joost Helsen, Andre B. de Haan. Capacitive deionization for water treatment: Screening of key performance
parameters and comparison of performance for different ions. Desalination 328, (2013) 8-16.
2. Celine Huyskens, Joost Helsen, Wim J. Groot, André B. de Haan. Membrane capacitive deionization for biomass hydrolysate
desalination. Separation and Purification Technology 118 (2013) 33–39.
FEM geometry of an experimental CDI cell
112
Is solution chemistry responsible for clay particle mobility through soil pores?
Van den Bogaert, R.1, 2, Labille, J.1, Cornu, S.2
Aix-Marseille Université, CNRS, IRD, CEREGE UMR 7330, F-13545 Aix en Provence
INRA, UR 1119 Géochimie des Sols et des Eaux, F-13100 Aix en Provence, France
Corresponding author: [email protected]
Clay particles mobility in soil is responsible for preferential transfer of various contaminants and for the
soil textural differentiation at the pedological time scale. The aggregation and dispersion mechanisms of
clay particles are expected to play a major role in this transfer. However, these mechanisms have mostly
been studied for pure and well-crystallized “model” clay minerals, and through wide physico-chemical
conditions, poorly representative for those encountered in soils.
In this work, we studied the respective impacts of pH and salt concentration on the colloidal behavior of
pedogenetic smectite particles originating from a Luvisol. Both static and dynamic approaches were used
considering (i) a time lapse of 1 to 5 hours that corresponds to the duration of a physico-chemical perturbation caused by infiltration of gravitational water along a rain event; (ii) a pH range of 4 to 8; and (iii) CaCl2
concentration range from 10-5 to 10-3 M, in order to be representative for the conditions encountered in
the soil solution. Aggregation and dispersion kinetics were measured by time resolved laser diffraction,
complemented with electrophoretic mobility analyses. The structural organization of clay particles and
aggregates was studied using X-ray diffraction, cryogenic SEM and static light scattering. Finally, percolation experiments through saturated diffusion columns were attempted to estimate the role of these
physicochemical interfacial reactions on the behavior of clay particles at the scale of the porous medium.
Based on these experiments, we drawn a phase diagram for soil clays as a function of pH and calcium
concentration, and identified the mechanisms and kinetics associated to the formation of the respective
states. We showed that soil particles behavior in suspension is similar to that recorded for model clays;
and that the aggregation and dispersion mechanisms related to pH and/or calcium modification are enough rapid to occur through the time scale of gravitational water (with the exception of dispersion induced
by salt dilution), and thus within soil porosity. Considering the overall soil system, these physico-chemical
processes have to be balanced with additional driving effects such as rainfall intensity and frequency and
inhomogeneous pore structure, both leading to varying active porosity.
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Acknowledgment
Funding program: ANR 10 Blanc 605 – Agriped
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113
Sorption of tylosin on goethite
Chen Yang1,2, Xuetao Guo1 and Zhi Dang1
1 College of Environment and Energy, South China University of Technology,
Guangzhou, China 510006
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2 Research Station Agroscope Reckenholz-Tänikon ART, Zurich, Switzerland 8046
Tylosin (TYL), a widely used veterinary antibiotic, was often employed ad feed additives in poultry and
swine farms. During the application of livestock wastes on agricultural fields, TYL might be persistent in
soils or transport to groundwater and contribute to the growth or development of antibiotic-resistant
microbial populations [1], it was necessary to understand the fates of such antibiotics in environmental
systems. Prior studies revealed that the fate and transport of antibiotics in the environment would be
affected by the interactions between chemicals and soil minerals [2]. In order to understand the contribution of goethite on the environmental fate of TYL and assess the sorption behavior and mechanism of TYL
on goethite accurately, we investigated the influences of solution chemical factors (pH and ionic strength)
on the sorption of TYL on goethite through a series of batch experiments. The sorption data were fitted
by Freundlich model and dual mode sorption model. It was obvious that sorption was strongly dependent
on pH and ionic strength. Sorption capacity of TYL increased as the pH increased and ionic strength decreased. The pH and ionic strength-dependences might be related with the specific complexation between
cationic/neutral TYL and goethite. Spectroscopic evidence indicated that tricarbonylamide and hydroxyl
functional groups of TYL might be accounted for the sorption on mineral surface. The experimental data
of TYL sorption could be fitted by surface complexation model (FITEQL), indicating that ≡FeOH with TYL
interaction could be reasonably represented as a complex formation of a monoacid with discrete sites on
goethite. It should be noticed that the heterogeneous of sorption affinity of TYL on goethite at various
environment to assess its environment risk.
References
1. Klare I, Konstabel C, Badstübner D, et al. Occurrence and spread of antibiotic resistances in Enterococcus faecium. International
Journal of Food Microbiology. 2003, 88: 269-290.
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2. Gao Y, Li Y, Zhang L, et al. Adsorption and removal of tetracycline antibiotics from aqueous solution by graphene oxide. Journal
of Colloid and Interface Science. 2012, 368: 540-546.
Acknowledgment
The was financially supported by the China National Science Fund Program (NO.41072268, 41173104) and Pearl River Young Scientist
Project of Guangzhou (2011J2200060).
114
Effect of pyrite interface on silver and mercury behavior in natural porous media
Delphine Charrière1,2, Manuel de A. Hernàndez Cortàzar3, Grégory Cohen1,2, Philippe Behra1,2
1. Université de Toulouse; INPT, LCA (Laboratoire de Chimie AgroIndustrielle); ENSIACET, 4, Allée Emile Monso, BP44362, F-31030
Toulouse Cedex
2. INRA; LCA (Laboratoire de Chimie AgroIndustrielle); F-31030 Toulouse
3. CMPL (Centro Mexicano Para la Producción más Limpia), Instituto Politecnico Nacional, Av. IPN s/n, Unidad Profesional Adolfo
López Mateos, Laboratorio Pesado E.S.F.M., Zacatenco, 07738 Mexico, D.F., México
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Interactions of heavy metals at liquid-solid interfaces have been largely studying by the scientific community due to their crucial role for understanding environmental pollution owing to the various human
activities: metallurgy, dentistry, chemistry, nuclear industry, paint and batteries, and agricultural habits. To
prevent migration of heavy metal pollutants in wastewater, contaminated soil and solid wastes, knowledge of mechanisms controlling transport and transfer of metals which occurs at the solid-liquid interface is
thus a prerequisite. Possible mechanisms are numerous: precipitation, dissolution, sorption, complexation, redox, etc. In subsurface environment, sulfide compounds such as pyrite are very often present. Due
to their high surface reactivity and their redox properties they can thus control the fate of trace elements
even when this mineral is present at low concentration. For better understanding its role, batch and column experiments were performed in the presence of silver or mercury with natural porous media, quartz
sand and schist, which both contained some pyrite. From experimental results with natural materials, we
observed a strong pH-control by pyrite in the first part of experiments due to its redox dissolution with
high release of Fe. After some delay, the presence of calcite buffers the pH due its dissolution too. At the
same time, we showed that sorption of Ag(I) is kinetically limited. At equilibrium, Ag(I) sorption behavior
depends strongly on pH with isotherm shapes characteristic of Langmuir-type relationship. From speciation calculations, Ag(I) sorbs mainly on iron (hydr)oxides and silanol surface sites. On the other hand, strong
complexes between Ag(I) and thiosulfates are formed due to oxidative dissolution of pyrite contributing
to decreasing Ag sorption capability. SEM-EDS analyses highlighted the surface complexation-precipitation of Ag2S and Ag(0) colloids which confirmed the important role of pyrite on Ag(I) speciation. On the
contrary, mercury which is sorbed at the pyrite interface blocks the surface site oxidation: no change in
the oxidation state of Hg(II) was observed. From all the experiments and XPS surface analyses, we showed
that depending on the type of metal which is present, surface reactivity of pyrite can change by increasing
either adsorption or redox precipitation of trace metals.
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115
Keynote
Flow-through electrode capacitive desalination and
experimental characterization of desalination electrodes
Matthew E. Suss
1. Department of Chemical Engineering, MIT, Cambridge, MA, USA
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2. Faculty of Mechanical Engineering, Technion - Israel Institute of Technology, Haifa, Israel
Capacitive deionization (CDI) is a novel approach to water desalination which is attracting significant and
growing research attention [1,2]. A CDI cell typically consists of two porous carbon electrodes between
which feedwater flows through an open channel or porous dielectric separator [3]. Charging the electrode
pair to a voltage difference of approximately 1 V causes salt ions in the feedwater to transport to, and
be electrostatically held against, oppositely charged carbon surfaces. In this lecture, I will describe the
development of what we termed “flow-through electrode capacitive desalination” [4]. In this system, the
feedwater flows directly through the porous electrodes themselves rather than between the electrodes.
While flow-through electrodes for desalination were first proposed in the 1970’s [5], the systems developed at that time suffered from electrode degradation and limited performance. Now, 4 decades later, we
have developed a novel, high performance flow-through electrode capacitive desalination system utilizing
newly developed hierarchical carbon aerogel monolith electrodes. The pore structure of this electrode
material is designed to allow for simultaneously high salt sorption and efficient fluid flow-through. I will
describe the physical principles and prototype results demonstrating that flowing through (rather than
between) the electrodes enables significant advantages in both desalination time and feed concentration
reductions.
Wednesday
a)
b)
c)
Figure 1: a) Schematic of the concept of flow through electrode capacitive desalination versus typical flow between
CDI cells. b) Porous electrode transport model results demonstrating the evolution of salt concentration in a complete
and charging CDI cell. c) A picture of our fabricated flow through electrode capacitive desalination prototype.
116
In the second part of the lecture, I will discuss our recently developed experimental techniques to characterize and study CDI cell and porous electrode performance. Characterization of CDI systems typically involves measurements of the downstream (treated) water conductivity [1,2,3]. However, the conductivity
data obtained can often be dependent on a large number of system and flow parameters, and is not well
suited to detect effects such as variations in sorption performance between electrodes. We have developed several unique tools which allow for improved and more insightful studies of CDI systems, and thus
can be used to catalyze future performance improvements. These include a first time measurement of
spatially resolved chloride salt concentration between charging electrodes in a CDI cell (using fluorescent
microscopy), and a framework for electrochemical impedance spectroscopy (EIS) studies of multiscale
porous electrodes [6,7]
References
1. Porada, S., et al. “Review on the Science and Technology of Water Desalination by Capacitive Deionization.” Progress in Materials
Science (2013).
2. Oren, Yoram. “Capacitive deionization (CDI) for desalination and water treatment—past, present and future (a review).” Desalination 228.1 (2008): 10-29.
3. Farmer, Joseph C., et al. “Capacitive deionization of NaCl and NaNO3 solutions with carbon aerogel electrodes.” Journal of the
Electrochemical Society 143.1 (1996): 159-169.
4. Suss, Matthew E., et al. “Capacitive desalination with flow-through electrodes.”Energy & Environmental Science 5.11 (2012):
9511-9519.
5. A. M. Johnson, et al. The Office of Saline Water Research and Development, Progress Report No. 516, US Dept. of the Interior,
Publication 200 056, 1970.
6. Suss, Matthew E., et al. “In situ spatially and temporally resolved measurements of salt concentration between charging porous
electrodes for desalination by capacitive deionization.” Environmental science & technology(2014).
7. Suss, Matthew E., et al. “Impedance-based study of capacitive porous carbon electrodes with hierarchical and bimodal porosity.” Journal of Power Sources (2013).
b)
a)
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Figure 2: a) Theoretical predications and direct measurements of spatially resolved salt concentration between charging porous electrodes of a CDI cell. b) Circuit model predictions
(black lines) and measurements (black dots) of the impedance of porous electrodes with
multi-scale pore structures for CDI.
117
Enhanced energy efficiency in increased discharging voltage Capacitive Deionization
T. Kim,1,2 J.E. Dykstra,1,3,* S. Porada,1 A. van der Wal,3 J. Yoon,2 P.M. Biesheuvel1,3
Wetsus, centre of excellence for sustainable water technology, Oostergoweg 7, 8911 MA Leeuwarden, The Netherlands.2School of
1
Chemical and Biological Engineering, Institute of Chemical Processes, Seoul National University, Daehak-dong, Gwanak-gu, Seoul
151-742, Republic of Korea. 3Department of Environmental Technology, Wageningen University, Bornse Weilanden 9, 6708 WG Wa-
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geningen, The Netherlands.
Capacitive deionization (CDI) is an electrochemical method for water desalination employing porous carbon electrodes. In the porous carbon electrodes, electrical double layers are formed, which consist of two
phases: the electron conductive matrix, in which electrons are stored, and the diffuse layer, in which ions
are stored to compensate the electrical charge. During the adsorption phase, electrons are transported
from the negatively polarized electrode towards the positively polarized electrode. To keep the electrodes
electroneutral, for every electron transported, a counterion is adsorbed into the diffuse layer or a co-ion
is desorbed from the diffuse layer, see Fig. 1. The desorption of these co-ions results in a charge efficiency,
that is the ratio of salt adsorbed over the electrons transported from the positively polarized to the negatively polarized electrode, below unity. A charge efficiency below unity results in higher energy demands,
because more electrons are transported per salt molecule removed from the brackish water, and is therefore disadvantageous.
We show how the charge efficiency can be increased by increasing the discharging voltage, such that we
can avoid the adsorption of co-ions in the porous carbon electrodes during the desorption phase. Consequently, these ions cannot be desorbed during the adsorption phase either.
We conducted experiments employing electrodes made of commercially available microporous activated
carbon. We applied a constant charging voltage of 1.2 V during the adsorption phase and different constant discharging voltages from 0 V up to 0.9 V during the desorption phase. Our experiments were conducted in flow-by mode, that is, the water flows through a spacer channel in between the two oppositely
polarized electrodes. The adsorption and desorption time of all the experiments was 1200 s, so that, at
the end of each adsorption and desorption phase, there was no net transport of electrons and ions to and
from the electrodes. We cycled three times through the adsorption and desorption phase before actually
collecting the data, so the salt adsorption and the charge density did not differ between one and the other
cycle. The experiments were performed with three different inflow concentrations of NaCl: 5, 20 and 80
mM. We compared the experimental data of the salt adsorption and the charge density with theoretical
calculations using the modified Donnan model [1].
e-
+++ Electrode +++ +
OR
Brackish
water
+
--- Electrode ---
OR
Potable
water
-
Figure 1 CDI cell during the adsorption phase. Every electron transported from the
negatively polarized electrode to the positively polarized electrode results in the
adsorption of a counterion into or the desorption of a co-ion from both oppositely
polarized porous carbon electrodes.
References
1. S. Porada, R. Zhao, A. van der Wal, V. Presser, and P. M. Biesheuvel, Progress in Materials Science 58, 1388 (2013).
118
Seawater Desalination and Energy Recovery using Flow-electrode Capacitive
Deionization (FCDi)
Sung-il Jeon, Jong-Soo Park, SeungCheol Yang, Jiyeon Choi, Jeong-gu Yeo and Dong Kook Kim
Korea Institute of Energy Research, 152 Gajeong-ro, Yuseong-gu, Daejeon 305-343, Republic of Korea.
Fax: +82 42 860 3152; Tel: +82 42 860 3133; E-mail: [email protected]
The energy-efficient capacitive deionization (CDI) techniques have been used for desalination of low salt
concentration water below brackish water and are not utilized for the seawater desalination, because it
has a limited ion adsorption capacity of the fixed porous carbon electrode. To overcome the limitation of
current CDI systems, we designed flow-electrode capacitive deionization (FCDi) system that uses flow-electrode. The flow-electrode, which is comprised of carbon suspension of activated carbon and 0.1 M NaCl
solution, flows through a flow-path carved on the current collector instead of the fixed carbon electrode
of the conventional CDI. FCDi unit cell exhibited continuous desalting performance more than 95 % of removal efficiency with respect to not only 32.1 g L-1 of NaCl solution but also 2.0 g L-1 of concentration. This
result demonstrates that the flow-electrodes, fed in the FCDi cell, have infinite ion adsorption capacity and
allow continuous seawater desalination. Also, we observed that energy supplied during charge step can
be recovered by constant current discharge of flow-electrode, which is fully charged at various voltages.
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119
Labilities of aqueous nanoparticulate metal complexes
Raewyn M. Town
Department of Physics, Chemistry and Pharmacy, University of Southern Denmark, Campusvej 55, DK-5230 Odense, Denmark.
[email protected]
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An inherent property of a dispersion of charged nanoparticles (NPs) is that their charges and reactive sites
are spatially confined to the particle body which is at a potential different from that in the bulk medium.
This feature has important consequences for the reactivity of nanoparticulate complexants: the diffusive
rate of reactant supply is lower as compared to molecular complexants, whilst the local concentration
of reactant ions may be enhanced if the particle’s electric field has the opposite charge sign. Thus the
uptake and release kinetics of small ions and molecules by NPs can differ significantly from those with
molecular ligands, or larger colloidal entities.1 These effects are most dramatic for soft NPs, for which the
electrostatic accumulation mechanisms operate on a 3D level.2 Accordingly, appropriate theory is needed
to describe and predict the lability of nanoparticulate complexes, i.e. the extent to which nanoparticulate
compounds may dissociate to release free target compounds which then contribute to signals measured
by dynamic speciation sensors, uptake by organisms, or accumulation at reactive interphases. The notion
of lability is inherently linked to the timescale of the process under consideration. A theoretical framework
is presented that describes the lability of metal-NP species over a range of effective timescales. The concepts are illustrated by electrochemical stripping data on metal complexes with natural soft nanoparticles
of humic acid.3
References
1. van Leeuwen, H. P.; Buffle, J. 2009. Chemodynamics of aquatic metal complexes: from small ligands to colloids. Environ. Sci.
Technol. 43, 7175-7183.
2. van Leeuwen, H. P.; Buffle, J.; Duval, J. F. L.; Town, R. M. 2013. Understanding the extraordinary ionic reactivity of aqueous nanoparticles. Langmuir, 29, 10297-10302.
3. Town, R. M.; van Leeuwen, H.P. 2014. Labilities of aqueous nanoparticulate metal complexes in environmental speciation ana-
Wednesday
lysis. Environ. Chem. in press.
120
Wastewater effects on soil-organic compound interactions, non-typical sorption
isotherms and clay vs. SOM as sorbing phases
Yonatan Keren, Nadezhda Bukhanovsky, Mikhail Borisover
Institute of Soil, Water and Environmental Sciences, The Volcani Center, ARO, Bet Dagan, POB 6, 50250, Israel
Wednesday
Soils are well-known to act as natural barriers preventing the contamination spreading and, therefore,
may accumulate pollutants. Drastic soil pollution may be induced by wastewater from olive oil production
(olive oil mill wastewater, OMW). The OMW land disposal affects the soil/water environment by inducing
toxicity, contaminating ground- and surface water sources, reducing soil wettability and changing multiple
physic-chemical soil properties. On the other hand, due to extremely high organic matter (OM) contents of
OMW, the OMW-soil interactions may provide important environmental-agricultural extreme scenarios of
wastewater effects on soil properties. Examining sorption of organic compounds from water on soils affected by OMW may provide an important mechanistic information on changes in soil surfaces and interfaces
and also be essential for prognosis of behavior of various organic pollutants (and agrochemicals) in the
soil environment. This presentation reports the selected results of the trilateral DFG-funded study on the
effects of OMW applied to a series of soils on soil sorptive efficacy towards organic compounds and examines (a) the possible sorption mechanisms and (b) the important sorptive components of soils. Among
others, organic compounds included typical herbicides, simazine and diuron, representing widely used
agrochemicals, and the OMW-soil interaction scenarios involved the various types of OMW application,
from the lab-controlled to the short-term field- or long-term scenarios. In multiple cases, the prior OMWsoil interactions involved distinct increases in sorption distribution coefficients of organic compounds thus
indicating an enhanced role of soils as barriers against environmental spreading of organic pollutants. Surprisingly, there were no distinct relations between the OMW-induced changes in distribution coefficients
of organic compounds on soils and the changes in soil organic matter (SOM) content. Variable shapes of
sorption isotherms were obtained for organic sorbates on soils, and, in some cases, sorption isotherms
demonstrated a sigmoid shape (Figure) which suggested cooperative interactions of sorbates with the soil
sorbents. However, the presence of a sigmoid shape was not related necessarily to the prior OMW-soil
interactions. Observed cooperative sorption expressed by a stepwise change in an isotherm might reflect
the changes in the soil matrix including both SOM and clay components. The data analysis suggested the
significance of the soil’s mineral clayey fraction for sorption of agrochemicals from water. In this way, the
consideration of SOM as a major soil sorbent for multiple non-ionized organic compounds, and, specifically for agrochemicals - herbicides, seems to be challenged.
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Sorbed Concentration (mg/
Kg)
200
150
100
50
0
0
5
10
15
Solution Concentration (mg/L)
Figure. Diuron sorption isotherm on loamy sandy soil
affected by OMW
121
Arsenic Adsorption: Effect of pH, Natural Organic Matter and Oxides Composition
Liping Weng
Department of Soil Quality, Wageningen University, P.O. Box 47, 6700 AA,
Wageningen, The Netherlands
Wednesday
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Surface complexation (adsorption) reactions strongly influence behavior of arsenic in the natural environment. For oxyanions, metal (hydr)oxides and clay edges are the most important reactive surfaces in nature. Arsenate (As(V)) binds much stronger than arsenite (As(III)) to the surfaces of metal (hydr)oxides. In
addition to arsenic speciation, the adsorption is also controlled by pH, calcium and phosphate adsorption,
presence of natural organic matter (NOM), and composition and reactive surface area of the surface. Due
to this complexity, results obtained from single component system cannot be directly applied to predict
arsenic adsorption in natural samples. In this case, advanced surface complexation models are powerful
tools in understanding and predicting behaviour of pollutants such as arsenic in the environment.
The pH dependent solid-solution distribution (solubility) of arsenic in five Dutch soil samples spiked with
arsenate was measured in the pH range 4–8, and the results were interpreted using the LCD (Ligand and
Charge Distribution) adsorption modeling. The Ligand and Charge Distribution model (LCD) combines surface complexation models for both oxides and natural organic matter, which allows for consistent description of multi-component adsorption to oxides, and takes also into account the effect of natural organic
matter that is present on oxide surface.
(1) Arsenic in soil shows a minimum soluble concentration around pH 6–8. This pH dependency can be
successfully described with the LCD model and it is attributed mainly to the synergistic effects from Ca
adsorption. In the presence of bivalent cations (e.g. Ca2+), solubility of arsenate is the lowest around neutral pH.
(2) Presence of natural organic matter adsorbed on the surface competes strongly with arsenic and significantly increases arsenic solubility. A change in the organic matter loading will therefore lead to a change
in arsenic distribution.
(3) Arsenic adsorption in soils depends on the relative contribution of aluminum and iron (hydr)oxides to
the total amount of metal (hydr)oxides. With increasing contribution from aluminum (hydr)oxides, adsorption of arsenic becomes weaker, whereas adsorption of phosphate is not so much influenced by the
change in oxides composition. Therefore solubility of arsenic is expected to be higher in aluminum (hydr)
oxides dominated systems than in iron (hydr)oxides dominated systems.
Fig. 1. Soluble arsenic and phosphate in one soil sample (Soil
2). Symbols are data and lines are model calculations.
122
Retention and Remobilization of Stabilized Silver Nanoparticles in Soils
Erwin Klumpp1, Yan Liang1, Scott A. Bradford3, Jiri Simunek4, Marc Heggen2, and Harry Vereecken1
1Institue of Bio- and Geosciences, Agrosphere (IBG-3), 2Ernst Ruska-Centrum ER-C, Research Center Jülich, Jülich/Germany
3United States Department of Agriculture, Agricultural Research Service, U. S. Salinity Laboratory, 4Department of Environmental
Sciences, University of California, Riverside/USA
Transport and retention of surfactant stabilized AgNP under environmentally relevant conditions was investigated by water-saturated columns packed with quartz sand and by undisturbed loamy sand soil columns with around 90% water saturation. The remobilization of retained AgNP from undisturbed soil was
studied by changing the solution chemistry such as change of cation types and ionic strength reduction.
Results of transport experiments in quartz sand and soil showed similar trends with regard to the effects
of physicochemical factors, e.g., enhanced transport with decreasing solution IS, increasing AgNP input
concentration and flow velocity. In contrast to the conventional filtration theory, retention profiles (RPs)
in sand exhibited uniform, nonmonotonic, or hyperexponential shapes that were sensitive to physicochemical conditions, while significant retardation of AgNP breakthrough and hyperexponential RPs were
observed in almost all the transport experiments with soil. Results from remobilization experiments indicated that further release of AgNP and clay from the soil was induced by cation exchange (K+ for Ca2+) that
reduced the bridging interaction and IS reduction that expanded the electrical double layer. Transmission
electron microscopy, energy-dispersive X-ray spectroscopy, and correlations between released soil colloids
and AgNP indicated that some of the released AgNP were associated with the released clay fraction.
References
1. Liang, Y., Bradford S.A., Simunek, J., Heggen M., Vereecken H., Klumpp E.: Retention and Remobilization of Stabilized Silver Nanoparticles in an Undisturbed Loamy Sand Soil. Environ. Sci. Technol., 47(21) (2013) 12229–1223
2. Liang, Y., Bradford S.A., Simunek, J., Vereecken H., Klumpp E.: Sensitivity of the Transport and Retention of Stabilized Silver Nanoparticles to Physicochemical Factors. Water Research, 47 (2013) 2572-2582
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123
The role of soil-borne DOC on the aggregation of synthetic Ag nanoparticles in soils
Sondra Klitzke1, George Metreveli2, and Friederike Lang3
1Chair of Soil Ecology, University of Freiburg, Freiburg im Breisgau/Germany; Department of Soil Science, Berlin University of Technology, Berlin/Germany; www.bodenkunde.uni-freiburg.de
2Deptartment of Soil and Environmental Chemistry, Institute of Environmental Sciences, University of Koblenz-Landau, Landau/Germany; http://www.uni-koblenz-landau.de/landau/fb7/umweltwissenschaften/uchemie
3Chair of Soil Ecology, University of Freiburg, Freiburg im Breisgau/Germany; www.bodenkunde.uni-freiburg.de
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Synthetic inorganic nanoparticles (NP) enter the soil through different pathways, where their stability is
affected by various processes. Sorption to silica surfaces is reported to decrease with increasing negative
particle charge (Thio et al., 2012). Several publications indicate an increased NP stability following DOC
sorption (Lecoanet et al., 2004). Therefore, we tested the following hypothesis: (A) Bare AgNP show stronger sorption to soil particles than those stabilized through additional charges. (B) The colloidal stability of
NP is increased through the sorption of soil-borne DOC. (A) We conducted batch experiments using silt
and differently stabilized (bare and citrate-coated (i.e. additionally charge stabilized) AgNP) AgNP at pH
6.5 and initial Ag concentrations (c0) ranging from 30 to 500 µg/L. After 24 h of end-over-end-shaking and
filtration (1.2 µm) the Ag concentration (cAg) was determined in the filtrate. The concentration of sorbed
Ag was determined through the difference between c0 and cAg. Results of both NP showed sorption curves
with similar slopes, suggesting that particle charge does not control sorption. (B) Bare and citrate-stabilized AgNP were suspended in a centrifuged soil solution (cut-off 10 nm). Zeta potential and sorbed
amounts of DOC were determined after 24 and 48 h. The optical density of the soil solution was determined at λ = 254 and 410 nm before and after DOC sorption. Results of bare AgNP showed high DOC sorption
after only 24 h along with an increase in particle charge and particle size. Short-chained DOC played a
more dominant role in sorption to AgNP than longer-chained DOC. In addition, aggregation kinetics of
citrate-stabilized AgNP were determined in suspensions with different AgNP concentrations following the
addition of (i) extracted soil solution and (ii) Ca-solution to obtain the same final concentration as in the
soil solution (1.5 mM Ca). While at 0.5 and 5 mg/L Ag, the two treatments did not differ significantly in
their particle size, at a Ag concentration of 10 mg/L, AgNP exposed to soil solution showed lower particle
sizes than AgNP exposed to Ca solution, suggesting that the stabilizing effect of DOC is relevant especially
at high AgNP concentration. Scanning electron micrographs are being prepared to further analyse the
state of aggregation as affected by organic ligands.
References
1. Lecoanet, H. F.; Bottero, J. Y. & Wiesner, M. R. (2004). Laboratory assessment of the mobility of nanomaterials in porous media.
Environmental Science & Technology, 38, 5164-5169.
2. Thio, B.J.R., Montes, M.O., Mahmoud, M.A., Lee, D.-W., Zhou, D.a, Keller, A.A (2012). Mobility of capped silver nanoparticles
under environmentally relevant conditions. Environmental Science & Technology, 46, 6985-6991.
124
Silver nanoparticle-based water treatment: mechanistic aspects and technology
viability
Di He and T. David Waite
School of Civil & Environmental Engineering, The University of New South Wales, Sydney, NSW 2052,Australia
A number of water treatment technologies based around use of silver nanoparticles are now on the market yet uncertainty remains as to their mechanism of operation, efficacy and long-term viability. Here
we summarise what is known of their mechanism of bactericidal activity, the factors determining their
lifetime and, from these insights, provide advice on the overall viability of the technology. In particular, attention is given to i) the impact of both the method of formation of the silver nanoparticles and nature of
the solid support on bactericidal activity with X-ray spectroscopic techniques used to determine the redox
state and molecular-level structure of the materials produced and ii) analysis of the factors contributing
the differences in both toxicity and longevity. In addition to insights into factors controlling oxidative dissolution kinetics and resultant production of silver ions (recognized to be a key determinant of toxicity),
attention is also given to factors that may contribute to Ag-mediated reactive oxygen species production
(He et al., 2011, 2013a,b).
References
1. He, D., Jones, A.M., Garg, S., Pham, A.N. and Waite, T.D. (2011). Silver nanoparticle - reactive oxygen species interactions: Application of an electron charging-discharging model. Journal of Physical Chemistry C 115(13), 5461–5468.
2. He, D., Ikeda-Ohno, A., Boland, D.D. and Waite, T.D. (2013a). Synthesis and characterization of antibacterial silver nanoparticle-impregnated rice husks and rice husk ash. Environ. Sci. Technol. 47, 5276-5284.
3. He, D., Bligh, M.W. and Waite, T.D. (2013b). Effects of aggregate structure on the dissolution kinetics of citrate-stabilized silver
nanoparticles. Environ. Sci. Technol. 47(16), 9148–9156.
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125
Ultrasound-assisted Preparation of Electrospun Carbon Nanofiber/graphene Composite
electrode for Capacitive Deionization
Gang Wang, Qiang Dong, Bingqing Qian, Jieshan Qiu*
Carbon Research Laboratory, Liaoning Key Lab for Energy Materials and Chemical Engineering, State Key Lab
of
Fine
Chemical,
School
of
Chemical
Engineering,
Dalian
University
of
Technology,
Dalian,
116024,
China.
E-mail address: [email protected] (Jieshan Qiu)
Website address: http://finechem.dlut.edu.cn/carbon/
The capacitive deionization technology (CDI) has drawn much attention because of its potential as an
energy-efficient alternative for producing fresh water from salted water sources. For the CDI technology,
the electrode materials with tuned pore structure and functionality such as conductivity are the key to the
efficient desalination process. In this talk, we report on the design and fabrication of electrospun carbon
nanofiber/graphene (CNF/G) electrodes by electrospinning polymer nanofibers, in which graphene oxide
was sprayed simultaneously, and the composites were heat-treated. The freestanding carbon nanofiber
web acts as a framework for sustaining graphene, and helps to prevent the agglomeration of graphene,
while the graphene helps to improve the conductivity of the as-obtained CNF/G composites that exhibit
an electrosorption capacity for NaCl of 15 mg/g, which is about 2.5 times of the adsorbed amount in the
case of the pristine CNF without graphene. This has demonstrated that the graphene is indispensible for
making high perforamnce CDI electrodes with desired structure and capacity.
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Keywords: Carbon fiber, Electrospinning, Graphene, Capacitive deionization
Wednesday
Figure 1 (a) Schematic of the electrospinning coupled with ultrasonic spray process, (b) top-view
and (c) side-view SEM images of
the as-prepared CNF/G, (d) SEM
image of the individual CNF/G fiber at higher magnification, and
(e) SEM image of the pristine CNF.
Figure 2 Desalination curves of
CNF and CNF/G electrodes as a
function of time in CDI, for which
the test conditions are: the cell
voltage, 1.2 V; the flow rate of water, 15 mL/min.
126
Capacitive deionization (CDI) of NaCl solution using activated carbon electrodes in a
novel CDI module
Qinghan Meng, Chunlei Meng, Ling Liu, Bing Cao
College of Materials Science and Engineering, Beijing University of Chemical Technology, 100029, Beijing, China
A novel CDI module is introduced using activated carbons as electrode in capacitive deionization process.
Voltage is not applied to each electrode as in the common CDI module but rather on the metal plate
outside the entire module. The effects of voltage and electrode pair number on the performance of the
novel CDI module are investigated, and the novel CDI module is compared with the common CDI module. The experimental results show the novel CDI module exhibits higher electrosorption capacity, shorter
desorption time, and lower energy consumption than those of common CDI module.
Keyword: Capacitive deionization, electrosorption, module
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127
Keynote
Salt removal, water recovery and energy consumption
in Membrane Capacitive Deionization
Albert van der Wala, b and Piotr Długołęckia
Voltea B.V., Wasbeekerlaan 24, 2171 AE Sassenheim, The Netherlands
Department of Environmental Technology, Wageningen University, Bornse Weilanden 9, 6708 WG,
Wageningen, The Netherlands.
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Membrane Capacitive Deionization (MCDI) is an emerging new electrochemical desalination technology,
which is suitable for the removal of ions from brackish water up to concentrations of about 100 mM
(ca. 5000 ppm). In MCDI ions are removed from feed water by applying an electrical potential difference
between two electrodes, whereby an ion-exchange membrane is positioned in front of each electrode.
Water can flow in the spacer compartment, which is situated between the oppositely charged electrodes.
Ions that are removed from the feed water are temporarily stored in the electrical double layers that are
formed at the electrode-water interface. In MCDI, the co-ions that are expelled from the electrical double
layers cannot enter the flow channel because they are blocked by the anion and cation exchange membranes. These co-ions are therefore retained in the interparticle space in the electrode compartment.
Because of charge neutrality these co-ions need to be compensation for by counterions, which pass the
ion exchange membrane from the spacer compartment. In MCDI, the expelled co-ions therefore lead to
an increase of the total ion storage capacity of the electrodes.
The electrodes need to be regenerated once they are saturated with ions, which can be done by reducing
or even reversing the applied voltage. In MCDI, the released counterions cannot migrate to the opposite
electrode, because of the presence of the ion exchange membranes. Therefore, during electrode regeneration high concentrations of salt ions can be obtained in the flow compartment, which can subsequently
be flushed out with a small amount of water, resulting in high water recoveries.
Dividing a feed-water stream into a dilute stream and a stream concentrated in ions costs energy and for
any desalination technology the energy consumption is a significant part of the Total Cost of Ownership.
In MCDI, the electronic charge is fully charge balanced by counterion adsorption and the charge efficiency,
which is the ratio of the ionic charge over the electrical charge, is therefore (close to) unity. As a consequence the energy use is directly proportional to the amount of ions that are being removed from the
feed water.
In this paper we discuss experimental results of a MCDI operation which shows how MCDI is ideally suited to achieve both high ion removal efficiency and high water recovery, which makes this an attractive
technology for many applications. Furthermore, we also present data for the energy consumption at different salt concentrations and salt removal levels. We demonstrate that up to 83% of the energy used for
charging the electrodes during desalination can be recovered in the electrode regeneration step. This can
be achieved by charging and discharging the electrodes in a controlled manner by using constant current
conditions. By implementing energy recovery as an integral part of the MCDI operation, the overall energy
consumption can be as low as 0.26 (kW·h)/m3 of produced water to reduce the salinity by 10 mM. In comparison, by using reverse osmosis under similar conditions the energy consumption is about 1kWh per m3
of produced freshwater. This means that MCDI is more energy efficient for treatment of brackish water
than reverse osmosis.
128
128
Posters
129
Posters
Poster Presentations Monday
Presenting author
Title
Page
1
Djamal Abdessemed
Treatment of the Pharmaceutical effluent by Membrane Bioreactor
132
2
Vytautas Abromaitis
Effect of granular size and activation level of activated carbon on ads- 133
orption and desorption of micropolutants
3
S. Bhuvanesh
Aerobic Granulation in a Hybrid Reactor
4
Mikhail Borisover
Soils as interfaces against pollution by PPCPs: the effect of sewage 135
sludge disposal
5
Sultana Boutamine
Interaction of metribuzin with zinc organometallic compounds
6
Wawan Budianta
Preliminary study of potential use of Central Java clay, Indonesia for 136
waste disposal liner
7
Andreas Bürger
Differences in the amino acid adsorption on relaxed and unrelaxed 137
magnetite-(111) and hematite-(001) surfaces
8
Toufik Chaabane
Electrochemical treatment for the surface industry wastewater
9
Laurent Duclaux
Adsorption studies of 4(tert-butyl)-1propylpyridinium bromide, ibu- 139
profen and 4(tert-butyl)-1(carboxyethyl)pyridinium bromide onto a
microporous activated carbon fabric
134
136
138
10 Lili Feng
Orthokinetic flocculation of PSL particles with polyelectrolytes at the 140
iso-electric point
11 Nina Gottselig
Elemental characterization of the fine colloidal and nanoparticulate 141
fraction in stream water from a forest catchment
12 Zakia Hank
Interaction of pesticides with some manganese-organic molecules 141
based frameworks
13 Xiaoqian Jiang
Speciation of phosphorus and colloidal Fe and Al (hydr)oxide com- 142
plexes in particle size fractions of an arable soil
14 Larysa Lysenko
Electroosmotic intensification of pressure driven dewatering
of FINE CLAY SLUDGE
15 Sandrina Meis
Computational adsorption experiments with Materials Studio 5.0 144
compared to GIXRD-results: The influence of Fe- and S- defect sites
on the adsorption model of H2O at the (100)-pyrite surface.
143
16 Chris Milne
Characterising silver nanoparticle stability in suboxic waters
17 Anna Missong
On the role of colloids and nanoparticles for the distribution of 146
phosphorus in a forest topsoil
145
18 Ines Mnif
Interaction of polyacrylamide flocculants and acrylamide with clays, 147
soil and sediments
19 K.B. Musabekov
Synthesis and characterization of magnetite/clay composites
148
20 Sabba Nassila
Interaction of Some Peticides with Iron Organometallic Compounds
149
21 Alba Otero
Retention of ionic pesticides at the soil–solution interface
149
22 Li Pengxiang
Adsorption of Anionic Surfactant on Silica
150
23 Tien Duc Pham
Adsorption characteristics of anionic surfactant and anionic dye onto 151
alpha alumina with small surface area
24 Benedicte Prelot
Performance of ionic MOFs on the capture of radionucleides
25 Benedicte Prelot
Dye adsorption at the TiO2/water interface and correlation with pho- 153
tocatalytic degradation
26 Gulmira Rakhymbay
Analysis of surface of the titanium electrode after precipitation of 154
indium
130
152
27 Alexandra Ribeiro
Potential of electrokinetic process for the remediation of estrogens 155
in soil
28 Alexandra Ribeiro
Potential of salt marsh plants for the remediation of organic com- 156
pounds
29 Zygmunt Sadowski
Effect of pH on adsorption of arsenic onto fly ash
157
30 Toshio Sakai
Removal of hypophosphite ions from water using ultrasound
158
31 Umarat
kasaem
Santisuk- Hydrodynamic behavior of Zero-valent Iron Permeable Reactive Bar- 159
riers: Effects of Permeability Loss
32 Wenfeng Tan
Protein complexation with Humic acids
33 Sagdat Tazhibayeva
Biocomposites on the base of yeast cells and diatomite such as sor- 161
bents of metal ions
160
34 Sagdat Tazhibayeva
Regulation of biodispersies stability by catonic polymers
35 Arnaud Villard
Decontamination of solution containing radioactive strontium by so- 163
dium nonatitante
36 Mingxia Wang
One-step synthesis of δ-MnO2 nanoparticles using ascorbic acid and 164
their scavenging properties to Pb(II), Zn(II) and methylene blue
37 Kenta Yamada
Effect of Soil Colloidal Properties on Surface Runoff from Tottori 165
Masa Soil
38 Gao Yingxin
The Mechanism of degradation on 4-Chlorophenol by Pulse Radio- 166
lysis
39 Miaoyue Zhang
Transport and retention of multi-walled carbon nanotubes in diffe- 166
rent porous media
40 He Zhao
Direct Electrochemistry of Horseradish Peroxidase based on Carbo- 167
nized Chicken Eggshell Membranes Materials
41 Sangho Chung
Development of Functionalized Graphene Electrode for Water Sof- 168
tening
42 Marta Hatzell
Enhanced energy generation with capacitive electrodes driven by 169
Exoelectrogen-generated ionic currents
43 Felix Hippauf
Solid-State NMR Studies on Adsorption of Electrolyte Ions in Carbon 170
Materials with well-defined Porosity
44 Mathijs Janssen
Temperature and size effects on the desalination of water
45 Doo-Hwan Jung
Preparation of Chestnut-like Carbon Electrodes for Capacitive Deio- 172
nization
46 Peter Kovalsky
Multidisciplinary modelling of CDI using optimisation tools: implica- 172
tions for agricultural applications
47 Dmytro Kudin
Water Denitrification using Energy-Efficient Capacitive Deionization 173
Technology
48 Xia Shang
Fabrication of composite capacitive deionization electrodes using 174
biochar materials and conductive membranes,
49 Nataliya Mishchuk
Electrokinetic remediation of fine clay soils contaminated by 175
Hydrophobic organic pollutants
162
171
Posters
131
Treatment of the Pharmaceutical effluent by Membrane Bioreactor
H.Benaliouche, D.Abdessemed
Laboratory of Sciences and Industrial Process Engineering, University of Sciences and Technology Houari Boumediene B.P., 32 El Alia
16111, Bab Ezzouar, Algiers, Algeria. E-mail: [email protected] . Tel: +213771851243
Posters
The issue concerning the presence and potential risks micro pollutants in the environment has become
a topical issue. Today, the wastewater treatment plants are not able to adequately treat this new type of
pollution. Eliminating pharmaceutical residues is possible with advanced technology using chemical and
physical processes such as membrane filtration, adsorption on activated carbon or advanced oxidation
processes. Currently, several studies are conducted to study and optimize the disposal of pharmaceuticals
by membrane bioreactor. The objective of this study is to evaluate the potential for the membrane bioreactor degradation pharmaceutical effluents containing high load of pollutants collected from different
sources. Proposed in the case of discharges from the manufacturing workshop ointment (mycoside molecule) in the case of the pharmaceutical plant. It was found that the pharmaceutical is loaded effluent carbonaceous pollution, nitrogen and phosphate. For the removal of these pollutants we opted for a coupling
of physico-chemical processes (coagulation flocculation), adsorption on activated carbon and membrane
bioreactor. The results showed the removal rate 96.86% of COD, 69.12% in turbidity, 59.48% in nitrate,
28.84% in nitrite and 58.70% in phosphate.
132
Effect of granular size and activation level of activated carbon on adsorption and
desorption of micropolutants
V. Abromaitis1,2, V. Racys1, R. Meulepas2
1–Kaunas University of Technology, Chemical faculty of Technology, Department of Environmental Engineering, Kaunas, Lithuania,
Radvilenu st. 19, LT-50254. E-mail: [email protected], [email protected]
2–Wetsus, Centre of Excellence for Sustainable Water Technology, Oostergoweg 7, 8911 MA Leeuwarden, Netherlands
Introduction. Pharmaceuticals and other micro-pollutants are not sufficiently removed during conventional wastewater treatment (Verlicchi et al., 2012). Activated carbon (AC) addition could form a solution
(Boehler et al., 2012), although the AC would need to be periodically replaced due to saturation. In Biological Activated Carbon (BAC) the AC is continuously regenerated though desorption and biodegradation.
This study investigates which type of carbon is most suited for BAC systems. The carbon should have a high
adsorption capacity and allow for desorption at the threshold concentration achieved by the microorganisms.
Materials and methods. Adsorption and desorption isotherms of pharmaceutical metoprolol (MET) on 9
types of special resin-derived AC were obtained. The AC varied in granular size and activation level (Table
1).
Table1 Matrix of AC used for adsorption/desorption experiments (AC dose 0.4 g/l)
Granular
Activation le-
Surface area,
Granular
Activation
Surface
size, μm
vel
m2/g
size, μm
level
area,
m2/g
Carbon 2 (C2)
250-355
40C
1200
Carbon 7 (C7)
1000-1400
20C
900
Carbon 3 (C3)
250-355
63C
1500
Carbon 8 (C8)
1000-1400
38C
1200
Carbon 4 (C4)
500-600
24C
900
Carbon 9 (C9)
1000-1400
58C
1500
Carbon 5 (C5)
500-600
40C
1200
Carbon 6 (C6)
500-600
63C
1500
Results and discussion. The isotherms corresponded to the Freundlich model: constants Kf and n are presented in Figure 1. The increased granular size of activated carbon resulted in decreased adsorption capacity. The transport through macro/mesopores to micropores was prolonged due to increased diameter of
activated carbon beads. The adsorption capacity was positively related to the activation level – due to the
larger surface area, developed during activation process in carbon dioxide environment.
Posters
Figure 1 Effect of granular size and activation level of AC for adsorption capacity (Kf) and intensity (n)
There was no clear correlation between granular size, activation level and adsorption intensity. For a given level of carbon saturation, the equilibrium concentration for desorption was circa 10 times lower than for adsorption. Therefore
these carbon types have a poor desorbability and are not suited for BAC applications.
References
Boehler M., Zwickenpflug B., Hollender J., Ternes T., Joss A., Siegrist H., 2012. Removal of micropollutants in municipal
wastewater treatment plants by powder-activated carbon. Water Science & Technology, 66, 2115-2121
Verlicchi P., Aukidy M. Al., Zambello E., 2012. Occurrence of pharmaceutical compounds in urban wastewater: Removal, mass load and environmental risk after a secondary treatment—A review. Science of the Total Environment, 429,
123–155
133
Aerobic Granulation in a Hybrid Reactor
S.Bhuvanesh* and T.R.Sreekrishnan
Waste Treatment Lab, Department of Biochemical Engineering and Biotechnology, Indian Institute of Technology Delhi, New Delhi,
Posters
India. E-mail: [email protected]
Anaerobic granulation has been studied for decades beginning with the use of Up-flow Anaerobic Sludge
Blanket (UASB) reactor for anaerobic treatment of wastewater. However the application of this technology
is greatly limited by drawbacks such as the inability to use it for nutrient removal and for treatment of
low strength wastewater. To overcome these weaknesses, recent research efforts have been dedicated to
developing aerobic granulation technology. Almost all recent studies on aerobic granulation have been on
sequencing batch reactors (SBRs).
The hybrid reactor (HAR), which uses self-immobilized microbial granules under fluidized conditions, was
developed at the Department of Biochemical Engineering and Biotechnology, IIT Delhi for biological treatment of wastewater. It combines the advantages of a UASB reactor and AFBR and has been successfully
used for the anaerobic treatment of wastewater and biological denitrification of wastewater. Unlike the
SBR, which includes batch fill-draw cycles, continuous operation is possible in an HAR. Moreover the operational sophistication in the HAR are closer to conventional treatment processes. Further the large gas–
liquid interface in the HAR reduces the required volume of air for aeration. Higher level of maintenance
associated with more sophisticated controls, automated switches, and automated valves as in a SBR is also
not required.
To study the aerobic granulation in the HAR for simultaneous
nitrification and denitrification, the reactor was aerated at the
rate of 0.2-0.3 vvm. Synthetic wastewater was used for the
study.
It was possible to achieve structurally stable granules within
45 days of reactor start-up. The diameter of the granules varied up to 4.5 mm with a mean diameter of around 3 mm. Our
previous studies on microbial granulation for denitrification
showed that the microbial flocs granulated within 15 days of
reactor start-up and had a mean diameter of 1.4 mm. The larger diameter granules in the aerobic reactor may have been
due to the spatial arrangement of the nitrifiers in the outer
sphere and denitrifiers in the inner core in the aerobic reactor.
The delay in the granulation may have been due to the higher
shear associated with aeration. Of the three reactors studied,
granulation was observed in reactor R1 and R2. However, the
granules formed in the reactor R2 were more prone to coagulation due to the low shear at the periphery
of the reactor. Results show the possibility of aerobic granulation in the hybrid reactor.
Table showing the effect of reactor geometry on granulation. A is the diameter of the cylinder. B is the
diameter of the inlet tube. C and θ are height and angle of the frustum cone.
134
Reactor
A (cm)
B (cm)
C (cm)
A/B Ratio
θ
Granulation
R1
4
1
3.5
4
23
+
R2
4
1
2.5
4
31
+
R3
4
1
1.5
4
45
-
Soils as interfaces against pollution by PPCPs: the effect of sewage sludge disposal
Alla Usyskin, Nadia Buhanovsky, Mikhail Borisover
Institute of Soil, Water and Environmental Sciences, The Volcani Center, ARO, Bet Dagan, Israel
135
Posters
Land application of treated sewage sludge is considered as an environmentally-meaningful solution of
a sludge disposal and may also positively contribute to the soil quality. However, the land application of
sewage sludge may become an additional pollution source in a soil-water interface due to the prior accumulation of pollutants in sludge in the wastewater treatment process. One important group of organic
pollutants termed Pharmaceuticals and Personal Care Products (PPCPs) may be accumulated in sewage
sludge, due to their low removal extent in wastewater facilities and hydrophobic properties, and therefore
reach the field, plants and water sources. When looking at variety of PPCPs compounds, hydrophobicity
and the acidic properties are often-found characteristics of the PPCP molecules that may strongly affect
their interactions with soils and control the further environmental fate. The study presented is focused
on two representatives of the PPCP family, triclosan and gemfibrozil, that are notable by their significant
concentrations in sewage sludge and also demonstrate a series of important biological effects, e.g, antibacterial triclosan is suspected to promote the development of antibiotics-resistant bacteria. Both organic
compounds behave as hydrophobic acids, and, therefore, their sorption behavior in soil environments is
also of general mechanistic interest. Therefore, in this work sorption kinetics and equilibria were studied
for both PPCPs on various soils incubated in the lab conditions with a series of sewage-sludge originated
amendments, in order to examine the capability of soil sorbents to provide an interface preventing the
further spreading of organic pollutants. The experimental data demonstrated that, following the soil – sewage sludge incubation, the sorption of both organic compounds by soil sorbents from water was strongly
increased, together with the soil organic carbon (SOC) content. This suggested that despite a significant
(triclosan) or almost full (gemfibrozil) ionization in solutions, soil organic matter (SOM) is the factor that
controls the interactions of a given PPCP acid in a series of soils studied at their typical pHs. The simple
consideration of SOM-triclosan (and -gemfibrozil) sorption interactions may be sufficient for evaluating
the environmental fate of the PPCPs studied. However, in comparing between organic sorbates, the extent
of ionization in aqueous solutions becomes a dominating factor in controlling sorption of hydrophobic
acids by soil sorbents. Importantly, for a given organic sorbate, there was no a single relation between
the sorptivity and the SOC content of the sorbents thus demonstrating (1) an impact of the SOM nature
on PPCP-soil interactions and (2) specifically, an enhanced sorptive potential of organic matter in sandy
soil sorbents as compared with other soils. The difference in sorptivity between soils might be related
to a less rigid SOM in sandy soils as compared with clay-containing soil sorbents. Interestingly, sorption
experiments on variously incubated sandy soils at different pHs suggested that interactions of molecular
and anionic forms of triclosan with sandy soil sorbents may be comparable. Therefore, as distinct from
a common wisdom, the sorption of organic anions by SOM sorbents may need to be taken into account.
Interaction of metribuzin with zinc organometallic compounds
Assia Boucifa, Zakia Hanka, Sultana Boutaminea and Djamal Abdessemedb
a
Université des Sciences et de la Technologie Houari Boumediene (USTHB), Faculté de Chimie, Laboratoire d’Electrochimie, Corrosion,
Métallurgie et Chimie Minérale, BP 32, El Alia, Bab-Ezzouar, 16111, Algiers Algeria. [email protected], [email protected]
bUniversité des Sciences et de la Technologie Houari Boumediene (USTHB), Faculté de Génie de Procédés, Laboratoire de Sciences,
Génie des Procédés et Environnement, BP 32, El Alia, Bab-Ezzouar, 16111, Algiers Algeria
Particular chemicals like pesticides which use, in agriculture, became inescapable are engendering an environmental pollution and more particularly that of soils.
It is urgent, for preservation of public health, to reduce at most our exposure to these substances and to
operate everything to reduce and control these pollutants. Some conventional adsorbing product such
carbon F400 are frequently used.
The adsorption on the synthetized metal organic complexes may be a alternate technique to disinfect soils
and waters polluted by pesticides and other chemicals.
In this context, some coordination compouds of Zinc were tested in the adsorption of mitrobuzin present
in contaminated water. The retained organic molecules are natural products (flavonoids and purines)
The preliminary results seems encouraging and we report them here.
Preliminary study of potential use of Central Java clay, Indonesia for waste disposal
liner
W.Budianta1), W. Prastistho1), J. Takemura2), H. Hinode2)
1)
Dept. Geological Engineering, Universitas Gadjah Mada
Jl. Grafika 2 Kampus UGM, Yogyakarta, Indonesia 55281. Tel. +62-274-513668
e-mail: [email protected]
2)
Tokyo Institute of Technology, Japan
Posters
Ookayama Campus 2-12-1, Meguro, Tokyo
The clay deposit in Central Java, Indonesia, is considered as a source for waste disposal liner do to their low
coefficient permeability and widespread distribution in Central Java. This preliminary study investigated
the geological, geotechnical and mineralogical properties of the founding clay in Boyolali, Central-Java region. The particle size distribution, specific gravity of the solids, and Atterberg limits, specifically the liquid
limit (LL), plastic limit (PL) and plasticity index (PI) were determined according to ASTM standard practice.
Mineralogical studies performed included the determination of the cation exchange capacity (CEC) and
mineralogical content of samples through the X-ray Diffraction (XRD) and Scanning Electron Microscope
(SEM) analysis. The result of this preliminary investigation show that our clay may be regarded as a suitable
material for waste disposal liner.
Keywords: clay, liner, permeability, mineralogy, waste disposal
136
Differences in the amino acid adsorption on relaxed and unrelaxed magnetite-(111)
and hematite-(001) surfaces
Andreas Bürger, Hermann Gies
Faculty of Geology, Mineralogy and Geophysics
Section Crystallography
Ruhr-University Bochum, Germany
Keywords: adsorption, iron oxides, force field simulation, amino acid
References
1. Fleet ME (1981) Acta Crystallogr B 37:917-920
2. Grünberg K, Müller EC, Otto A, Reszka R, Lindner D, Kube M, Reinhardt R, Schüler D (2004) Appl Environ Micro 70:1040-1050
3. Schüler D (2004) Arch Microbiol 181:1-7
4. Bürger A, Magdans U, Gies H (2013) J Mol Model 19:851-857
137
Posters
Magnetite (Fe3O4) crystallizes in the inverse spinel structure [1]. In nature magnetite is also an important biomineral. Magnetotactic bacteria, e.g., use magnetite single-crystals to orientate themselves in
the earth magnetic field. The connection between the inorganic magnetite and the organic parts of the
microorganism is the magnetosome membrane (MM). This membrane is built by membrane proteins
which are dominated by the amino acids aspartic acid (asp), glutamic acid (glu), glycine (gly) and leucine
(leu) [2,3]. Bürger et. al [4] showed that it is energetically favorable for the amino acids to adsorb on the
relaxed magnetite-(111)-surface. For the current study, the relaxed and unrelaxed hematite-(001) and the
relaxed and unrelaxed magnetite-(111) surfaces have been used. They are the most common surfaces
of the respective minerals. Their crystal structures contain iron as Fe3+ (hematite) and a mixture of Fe2+
and Fe3+ (magnetite). However, in all systems studied the surface oxygen termination is the dense packed
oxygen layer.
Force field simulations of the interaction distances between the iron oxide surfaces and the amino acid
offer the possibility to investigate if and how the amino acids interact with the surfaces. Additionally, it is
possible to investigate the interactions and the adsorption distances between the surface atoms and the
functional groups of the amino acids. We have chosen the COMPASS force field because all parameters
of the surfaces and of the amino acids are defined. As simulation software we used Forcite which is integrated in the Materials Studio 5.0 software package. The amino acids may adsorb in a docking box of 40.3
Å x 40.3 Å x 20 Å on the relaxed hematite-(001) surface, a docking box of 50.4 Å x 50.4 Å x 20 Å on the
unrelaxed hematite-(001) surface, a docking box of 47.5 Å x 47.8 Å x 20 Å on the relaxed magnetite-(111)
surface and in a docking box of 47.5 Å x 47.5 Å x 20 Å on the unrelaxed magnetite-(111) surface. The surface thicknesses are 12.5 Å, 13.2 Å, 7.4 Å and 7.3 Å, respectively. For every amino acid-iron oxide system
10,000 frames has been calculated, resulting in 120,000 frames altogether. The lowest energy systems for
each combination have been evaluated.
The comparison of results of the simulations shows the differences in the adsorptions behavior. The adsorption mode switches between monodentate, bidentate and bridging, depending obviously from the
amount of the iron cations and their oxidation state. The Fe-O adsorption distances between the surface
Fe-atoms and the amino acids O-atoms vary between the different adsorption systems, but in all different
cases the electrostatic interaction dominates the process. The conformations of all of the four amino acids
vary for the different iron oxide surfaces.
In our study we show that the behavior of the iron oxides surfaces take distinct influence on the adsorption distance, the binding mode and especially the conformation of the amino acids.
Electrochemical treatment for the surface industry wastewater
Zaîdi Sara(a), Toufik Chaabane(a,*), André Darchen(b) and Rachida Maachi (a)
(a)
USTHB / FGM-GP/Environmental department, BP 32 El-Alia 16111, Bab Ezzouar, Algiers, Algeria.
Tel : 21321247169
(b)
UMR CNRS n◦6226 Institut des Sciences Chimiques de Rennes, ENSCR, Avenue du Général Leclerc, CS 50837 - 35708 Rennes Cedex
7, France *
This study had like main aim the combination in the same cell of electrolysis two types distinct of treatment: the electroflotation (EF) and the electrochlorination (ECH), with an objective to eliminate the inorganic pollutants. At the time of this study, it was shown that with a wise choice of operating conditions,
the cell of EF presents an excellent performance for the elimination of heavy metals. The results obtained
showed that the EF is a method of separation effective for the copper reduction. Thus, it is possible to carry out rates of recoveries going up to 88.90 %, without chemical addition of additive. The examination of
the effect of the operational parameters shows that the initial pH is a determining factor in the EF process.
Indeed, it proves that a sufficiently high pH generates the formation of the flocs of good buoyancy what
contributes to the improvement of the effectiveness of the technique. Moreover, the rise in the intensity
of current makes it possible to decrease the processing time. For the treatment of the solutions Cu-EDTA
by EFF, one notes the remarkable effect of the presence of the EDTA. After the elimination of the copper
not complexes by EF of its precipitate, a quantity of complexes copper can be recovered with the cathode
by deposit according to the content of EDTA in the solution. Oxidation by ECH showed its effectiveness for
the elimination of the EDTA. Indeed, a total destruction of this pollutant can be obtained in the cell of EFF.
The study also showed that the electro-oxidation of the EDTA is ensured by active chlorine produces in
situ. In addition to the examination of the influence of the various factors made it possible to retain that
the intensity of current and the content chloride are two big factors in elimination by ECH. In addition, the
tests carried out on the mixed solutions Cu-EDTA, indicate that coupling EF-ECH makes it possible to eliminate the organic and inorganic pollutants simultaneously. Thus, this process can constitute an alternative
or a complement of the traditional methods. Moreover, this coupling presents a particular interest, because it seems to be perfectly adapted to the industry of the surface treatments, by reducing the capacity
complexion of the organic pollutants, which constitute a serious constraint for the treatment of this kind
of effluent, and by thus allowing the elimination of heavy metals. This not-conventional approach to the
treatment of the aqueous solutions containing of heavy metals gave promising results.
Posters
Keywords: Electrochemical treatment – wastewater – Copper – EDTA
138
Adsorption studies of 4(tert-butyl)-1propylpyridinium bromide, ibuprofen and 4(tertbutyl)-1(carboxyethyl)pyridinium bromide onto a microporous activated carbon fabric
Lotfi Sellaoui1,2, Hanen Guedidi1, Imadeddine Lakehal1, Jean-Marc Lévêque1, Laurence Reinert1,
Abdelmottaleb Ben Lamine2, Laurent Duclaux1,
Laboratoire de Chimie Moléculaire et Environnement, University of Savoie 73376 Le Bourget du Lac Cedex, France
Laboratoire de Physique quantique, Faculté des Sciences de Monastir, University of Monastir, Monastir 5000, Tunisia
*[email protected]
Ionic liquids (ILs) possess an array of properties which are extremely low vapour pressure, high thermal and chemical
stabilities and non-flammability that make them attractive for academy and industry. Initially, ionic liquids were considered environmentally friendly, but later, it has been stated that they show a wide range of environmental toxicities.
Despite a lot of advantages due to their physical and chemical properties and potential applications as green solvents
or electrolytes etc.., ILs are considered as emergent pollutants because their synthesis and their use at a large scale
may lead to their contact with aqueous media. For the removal of ILs from water and water streams, adsorption on
activated carbons is an important technology which is widely used now-a-days. In this work, we have compared the
adsorption properties of ibuprofen (IBP): a pharmaceutical molecule, and two pyridinium ILs in order to better understand their adsorption mechanism on an activated carbon fabric. The ILs were chosen and designed in order to obtain
organic cations with molecular size and chemical functionalities quite similar to the ones of ibuprofen.
H3C
a)
+
H3C
N
Br
CH3
CH3
b)
OH
CH3
CH3
H3C
Figure 1 Developed formulas of IL1 (a), Ibuprofen (b) and IL2 (c).
H3C
c)
O
+
HO
N
B
r
CH3
CH3
-
O
Two ILs : 4(tert-butyl)-1propylpyridinium bromide (referred to IL1) and 4(tert-butyl)-1(carboxyethyl)pyridinium bromide (referred to IL2) were synthesised in our laboratory by the reaction of 4-tert-butylpyridine with either 1-bromopropane or 3-bromopropionic acid to obtain IL1 and IL2, respectively. The reactions were conducted under magnetic
stirring, at room temperature for 24 hours. Products were then purified by successive washing in ethyl acetate. The
final ILs product were vacuum dried for 2 days under 10-3 mbar in order to remove the traces of solvent and stored
prior to their use under dried atmosphere. The activated carbon fabric (900-20 from Kuraray, Japan) was characterized by N2 adsorption-desorption at 77 K and CO2 adsorption at 273 K, pHPZC (point of zero charge) measurements and
acido-basic titrations (Boehm method).
The adsorption kinetics (C0= 0.4 mmol L-1) and isotherms of the single pollutants were studied at pH 3 (obtained by
addition of HCl) and 7.5 (pH maintained by a 0.04 M Na2HPO4/KH2PO4 buffer) in UHQ (Ultra High Quality) water (18.2
MΩ). All the batch kinetics and isotherms were investigated by shaking (250 rpm) at a given temperature (generally
25°C) stoppered flasks (30 mL solution) containing the fabric samples (10 mg). The adsorption kinetics of an equiof equimolar binary systems IL1/IL2, IL1/ IBP, and IL1/IBP were determined by the same protocol except the use of
25 mL solutions. The organic molecules in the filtrated solutions were analyzed by UV spectrometry and HPLC. The
adsorption isotherms of the molecules were studied at 13, 25 and 40°C; and the thermodynamic parameters (isoteric
enthalpies, entropies and Gibbs free energies) were determined. The pore size distributions of the carbons loaded
with the pollutants were determined by DFT simulations from gas adsorption isotherms, to investigate the porosity
accessible to each adsorbate.
The effect of pH influences strongly the adsorption uptake. The increase in pH from 3 to 7.5 affects the charge of IL2
as its organic cation (pKa=4.1) transforms in zwitterion (carboxylate group) but the charge of IL1 remains positive. As
increasing the pH from 3 to 7.5 the charge of the carbon fabric tends to decrease (pHPZC=8.5), inducing a decrease in
the electrostatic repulsion between the organic cations and the adsorbent that results in an enhanced uptake. The
competitive adsorption in ternary mixture and binary systems were tentatively explained in term of interaction with
adsorbent, and simulated in order to determine the thermodynamic parameters and to compare their values with the
ones for the single adsorbate adsorption.
139
Posters
molar mixture of the three adsorbates (each adsorbate at C0= 0.4 mmol L-1) was studied at pH=7.5. The isotherms
Orthokinetic flocculation of PSL particles with polyelectrolytes at the iso-electric point
Lili Feng1, Motoyashi Kobayashi, Yasuhisa Adachi
1
Motoyashi Kobayashi, Yasuhisa Adachi (Graduate School of Life and Environmental Sciences, University of Tsukuba, 1-1-1 Tennodai,
Tsukuba, Ibaraki, 305-8572, Japan)
Tel: 090-9801-0524
Posters
Aggregation rates of polystyrene latex particles (1956nm) induced by two positively charged polyelectrolytes, similar in the molecular weight (Mw= 5×106 g/mol) but different in the charge density (σ=1 and 0.04),
were measured by Coulter Counter at the isoelectric point as a function of the ionic strength.
In the case of the flocculation with the high charge density polymer, an accelerated rate of flocculation was
found at the isoelectric point for salt-free, 2.3 times faster than that of salt-induced rapid coagulation (observed with KCl 1M). The accelerated rate might be originated from the electrostatic attraction between
bare parts of one particle and polyelectrolytes covered parts of neighboring particles, i.e. patch. Due to
the screening electrostatic interaction with the increase of ionic strength the rate of flocculation decreases
with increasing ionic strength and becomes the same as that of salt-induced rapid coagulation at the ionic
strength of KCl 10mM.
In the case of the flocculation with the low charge density polyelectrolyte, an initial accelerated rate of
flocculation followed by a subsequent stabilization was observed for salt-free. The initial acceleration can
be explained by the formation of “bridges” between particles, and the stabilization should be ascribed to
the steric repulsions of adsorbed polyelectrolyte segments due to further adsorption/relaxation of polymer chains on the surface. With increasing ionic strength, the rate of flocculation decreases and even
becomes slower than that of salt-induced rapid coagulation. This trend indicates that the steric effect is
more profound at high ionic strength.
a)
b)
Figure 1 Temporal variation of the total number concentration of particles in the presence of polyelectrolytes (a) with
high charge density and (b) the low charge density.
140
Elemental characterization of the fine colloidal and nanoparticulate fraction in stream
water from a forest catchment
N. Gottselig1, R. Bol1, V. Nischwitz2, H. Vereecken1, E. Klumpp1
Institute of Bio- and Geosciences, Agrosphere (IBG-3)
1
Central Institute for Engineering, Electronics and Analytics, Analytics (ZEA-3)
2
Research Center Jülich, Wilhelm Johnen Str., 52425 Jülich, Germany
Email: [email protected], [email protected], [email protected], [email protected], [email protected]
Natural fine colloids and nanoparticles have the potential to encapsulate and bind nutrients. Their size
range and composition is therefore relevant to understand the transport of essential nutrients like phosphorus in an aquatic ecosystem. The aim of the study was to characterize fine colloidal and nanoparticulate bound phosphorus of distinct hydromorphological areas in stream water samples from a forested
experimental test site in a small headwater catchment. Asymmetric Flow Field Flow Fractionation (AF4)
coupled online to inductively coupled plasma mass-spectrometry (ICP-MS) was applied for size resolved
detection of phosphorus (P), iron (Fe), and aluminum (Al) in the fractions. Additionally, the dissolved organic matter (DOM) content was derived from the online UV signal. Two distinct fractions were detected and
characterized. For the first size fraction, variations in P concentrations strongly correlated to the course of
Al variations; in addition, high Fe presence in both fractions was accompanied by high P concentrations.
Moreover, DOM was detected with P in presence of Fe and Al. Possibly, Fe and Al containing particles are
carriers of P compounds and associated with organic matter. The study enables for the first time to trace
and conceptually define the inputs and source regions of fine colloidal and nanoparticulate fractions within a small river of a headwater catchment. The stream water investigations will be extended to additional
test sites and a broader range of elements.
Interaction of pesticides with some manganese-organic molecules based frameworks
Zakia Hank*, Assia Boucif*, Djamal Abdessemed** and Sultana Boutamine*
*Université des Sciences et de la Technologie Houari Boumediene (USTHB), Faculté de Chimie, Laboratoire d’Electrochimie, Corrosion,
Métallurgie et Chimie Minérale, BP 32, El Alia, Bab-Ezzouar,16111, Algiers Algeria. [email protected], [email protected]
**Université des Sciences et de la Technologie Houari Boumediene (USTHB), Faculté de Génie de Procédés, Laboratoire de Sciences,
Génie des Procédés et Environnement, BP 32, El Alia, Bab-Ezzouar,16111, Algiers Algeria
141
Posters
Particular chemicals like pesticides which use, in agriculture, became inescapable are engendering an environmental pollution and more particularly that of the waters as well of surfaces as ground-water sheets.
operate everything to reduce and control these pollutants.
So, the presence of pesticides in drinkable waters is severely regulated and the producing companies of
water, to conform to the established standards, are obliged to include in their networks of water treatment, processes to eliminate them.
The adsorption on the synthetized metal organic complexes may be a technique to disinfect waters polluted by pesticides and other chemicals.
In this context, some coordination compouds of manganese were tested in the adsorption of mitrobuzin
present in contaminated water. The retained organic molecules are natural products (flavonoids and purines)
The preliminary results seems encouraging and we report them here. They are compared to those obtained with a conventional adsorbing agent, namely powdered activated carbon F400.
Speciation of phosphorus and colloidal Fe and Al (hydr)oxide complexes in particle size
fractions of an arable soil
Xiaoqian Jiang1, Roland Bol1, Volker Nischwitz2, Sabine Willbold2, Erwin Klumpp1
Institue of Bio- and Geosciences, Agrosphere (IBG-3)
1
2
Research Center Jülich, Jülich/ Germany
E-mail: [email protected], r.bol@ fz-juelich.de, [email protected], [email protected]
Posters
Soil organic and inorganic phosphorus are in the majority of cases stabilized through the association with
mineral components, especially with Fe and Al (hydr)oxides. However, few studies have focused on the
relative contributions of different organic and inorganic forms of P bound to Fe and Al oxide colloids. In our
arable soil study, amorphous and crystalline minerals were separated by selective dissolution with oxalate
acid and dithionite–citrate from various particle-size fractions (>2000, 450-2000, 100-450, and 1-100 nm).
Asymmetric flow field-flow fractionation (AF4) coupled to inductively coupled plasma mass spectrometer
(ICP-MS), solution 31P-nuclear magnetic resonance spectroscopy (NMR) and transmission electron microscopy (TEM) were employed. They were used to examine the speciation and contribution of (inorganic and
organic) P bound to amorphous and crystalline Fe and Al (hydr)oxides in several soil fractions and to study
the mechanism behind P fixation to these colloids in arable soil.
Results showed that colloids and nanoparticles have higher amounts of Fe, Al and P than larger sized particles. P is, to a large extent, associated with amorphous Fe and Al (hydr)oxides. Soil nanoparticles <100nm
revealed two size fractions measured by AF4. The smaller size fractions (below 5nm) consist of natural
organic matter (NOM) with a high UV-absorbance and P content. The larger size fraction (approximately
60nm) is a complex of Fe and Al (hydr)oxides linked to P, clays and NOM. Furthermore, it is more likely that
the P absorbed to NOM is bound to crystalline rather than to amorphous Fe and Al (hydr)oxides.
142
Electroosmotic intensification of pressure driven dewatering
of FINE CLAY SLUDGE
Larysa Lysenko, Nataliya Mishchuk, Nikita Borovitskiy, Elena Rynda
Institute of Colloid Chemistry and Water Chemistry of National Academy of Sciences of Ukraine, bulv.Vernadskogo, 42, Kiev-142,
Ukraine, 03680, [email protected]
143
Posters
Dewatering of disperse systems is an important problem for consolidation of sludge occurring in treatment of waste and drinking water, as well as for mining, food, paper, pharmaceutical and other industries.
The most used methods include thermal drying, pressure and vacuum filtration, centrifugation and other
mechanical methods. However, thermal methods need high power consumption and efficiency of mechanical methods goes down when handling fine materials characterized by small particle sizes and low
hydrodynamic permeability (gel sewage sludge, different clayey waste, etc.). One of the ways to enhance
the mechanical methods is the use of combination of pressure driven dewatering with electroosmotic
one, for which the hydrodynamic permeability of the material is not a critical parameter, and the power
consumption is much smaller comparing with the thermal methods. At such combination of dewatering
factors the applied pressure not only squeezes the water, but also provides the contact of electrodes with
partially dewatered sludge preventing the rupture of electric circuit and, correspondingly, the cessation
of electroosmotic flow.
Efficiency of combination of pressure driven and electroosmotic dewatering is determined by combination
of two opposite factors. Firstly, to promote the compaction of sludge under action of pressure the electrostatic repulsion between the particles must be decreased, that is possible at the reduction of the surface
potential. Secondly, it is necessary to enhance the electroosmotic velocity of liquid flow through the sludge, i.e. to enlarge the surface potential of disperse particles. Since we have two contradictory conditions,
the optimization of dewatering process is rather complicated task, which requires a careful control and
regulation of the characteristics of particles and pore solution, and optimization of parameters of sludge
treatment.
The experimental investigations of the conditions necessary for enhancement of pressure driven dewatering were conducted using a model system based on the dispersion of kaolinite, which is fine clay material.
Since electrokinetic potential and, correspondingly, the velocity of electroosmosis depend on the equilibrium pH of pore solution, we performed detailed analysis of dispersion properties at different concentration of acid or alkali solutions introduced in the used dispersion. Particularly the magnitude and sign
of the zeta potential of disperse particles and the velocity of electroosmotic flow at different values of pH
were studied. In result of these investigations a sufficiently wide range of pore solution pH (9<pH<12),
wherein the electrokinetic potential of the kaolinite particles and the electroosmotic velocity of liquid
through kaolinite dispersion remain almost constant, was found. It is important to stress that the optimal
conditions for the electroosmotic component of dewatering depend not only on pH of introduced acid or
alkali solutions, but also on the equilibrium values of pH, which is defined by the buffer and ion-exchange
capacities of the dispersion. Large values of pH, i.e. high concentration of electrolyte, corresponds to the
case of relatively thin electrical double layer and, correspondingly, low energy barrier between the particles that should improve the compressibility of the dispersion, leading to the increase of the pressure
driven component of dewatering.
The experimental investigations of dewatering efficacy were performed at a few initial moistures of dispersion, different values of applied pressure, voltage and treatment time. The main regularities of dispersion compression and dewatering were obtained that allow predicting the optimum conditions of sludge
treatment.
Computational adsorption experiments with Materials Studio 5.0 compared to GIXRDresults: The influence of Fe- and S- defect sites on the adsorption model of H2O at the
(100)-pyrite surface.
Sandrina Meisa, Hermann Giesa, Uta Magdansc, Xavier Torrellesb
a Department of Geology, Mineralogy and Geophysics, Ruhr-University Bochum, Bochum (Germany). b Institut de Ciencia de Materials de Barcelona (ICMAB), Barcelona (Spain). c Institute for Physics and Astronomy, University of Potsdam, Potsdam (Germany.)
Posters
Chemical reactions at the (100)-pyrite (FeS2) surface play an important role in many environmental, geological and chemical processes, e.g. acid mine drainage, bacterial pyrite oxidation, oxidation in aquifers
and coal liquefaction and heterogeneous catalysis. During the last decades most studies about the pyrite
surface structure and its adsorption properties were carried out in order to study reaction mechanisms
and active sites involved in acid mine drainage processes. In this process the oxidation of pyrite leads to
the formation of sulfuric acid that could be problematic for the ground water cycle. To understand these
processes it is of essential importance to understand the adsorption properties of pyrite to organic molecules and water. The structures of the dry (100)-pyrite surface and the interface of the (100)-pyrite surface
with water were determined with grazing incidence X-ray diffraction experiments (GIXRD) previously1,2.
An adsorption model for water at the pyrite surface was determined including three adsorption layers, a
transitional zone of partial ordered water molecules and water molecules that occupy defect sites of the
topmost FeS2-layer.
In this study the adsorption model of water at the (100)-pyrite surface near iron and sulphur defect sites
is analysed and compared to experimental results. We present computational experiments, especially
molecular dynamic simulations using the forcefield COMPASS. The simulations were carried out with the
program package Materials Studio 5.0, particularly the program “Forcite”, from Accelrys Inc. The surface
cell structure determined previously from GIXRD experimental results was used as a start model for the
simulations. A surface area of 3x3 surface cells (16,25Å²) and a depth of 2,5 surface cells (13,5Å) of pyrite
was selected for the simulations. A vacuum slab of 30Å was added as adsorption region to permit enough
mobility of the H2O-molecules during the dynamic runs. Different amounts of iron and sulphur defect sites
were introduced to the topmost FeS2-layers of the surface during different simulation runs. Each dynamic
run was calculated for 200ps with a step width of 0.2fs. The geometry optimization includes the smart
method, using the Ewald-summation method for electrostatic and the atom based calculation method for
van-der-Waals interactions.
The introduction of sulphur defects to the surface model has a stronger influence to the H2O-adsorption model compared to the effect of iron defect sites. By introducing iron defects the adsorption model
shows no differences compared to a surface free of defects. Only partially a small decrease in the distance
between the topmost FeS2-layer and the first H2O-adsorption layer about 0.2-0.4Å was determined. The
sulphur defects show a stronger influence, as H2O-molecules could be observed in the topmost FeS2-layers occupying the defect sites of sulphur dimers. Additional adsorbed H2O-molecules occur between the
topmost FeS2-layer and the first H2O-adsorption layer that is located 2.0(3)Å above the topmost FeS2-layer.
These results are in good agreement with the previously determined experimental model from GIXRD-data, with molecular dynamic simulations after Philpott et al.3 and UHV-experiments carried out by Guevremont et al.4.
References:
1. Meis S, Magdans U, Torrelles X, Gies H. Mineralogical Magazine (2013), 77(5), 1733
2. Meis S, Magdans U, Torrelles X. Acta Cryst. (2011) A67, C338-C339
3. Philpott M R, Goliney I Y, Lin T T. J. Chem. Phys. (2004), 120(4), 1943-1950
4. Guevremont J M, Strongin, Schoonen M. A. Am. Mineral. (1998), 83, 1246–1255
144
Characterising silver nanoparticle stability in suboxic waters
C J Milnea, C N Elgyb, D C Gooddyc, D J Lapworthc, E Valsami-Jonesb
a
British Geological Survey, Keyworth, Nottingham, NG12 5GG
b
Facility for Environmental Nanoparticle Analysis & Characterisation (FENAC), University of Birmingham, Edgbaston, B15 2TT, UK
c
British Geological Survey, Wallingford, Oxon, OX10 8BB, UK
Corresponding author: C J Milne, [email protected]
Intensity (%)
Manufactured silver nanoparticles (AgNPs) are released into the aquatic environment from a range of
waste water from domestic, medical, industrial and manufacturing sources. The presence of colloidal Ag in
environmental samples has been known for some time, but has not been effectively characterised. Recent
studies have investigated in detail the impact of critical environmental parameters such as pH, elemental
composition, ionic strength and particle properties such as capping agents (AgNP stabilisers) on the behaviour of AgNP in idealised solutions and bacterial growth media.
The potential for the formation of AgNPs via reduction of Ag+ ions in the presence of humic acids (HA) has
been indicated in recent reports. Redox conditions play an important role in the stability of environmental
AgNPs; following contact with dissolved oxygen in water, AgNPs can degrade over time and release Ag+(aq)
ions; these may form AgCl particles, which in turn may agglomerate or be reduced back to AgNPs. Sulfidation also strongly affects surface properties of AgNPs, modifying surface charge and dissolution rate.
There is a common assumption that these are very stable and low in toxicity, however there is limited
experimental data to support this at present.
To date, very few studies have characterised AgNPs in suboxic environmental matrices using multiple techniques or investigated their fate/stability in realistic environmental matrices/AgNP concentrations. Using
Dynamic Light Scattering (DLS), Atomic Force Microscopy (AFM), Transmission Electron Microscopy (TEM)
and zeta potential, we have characterised citrate- and PVP-capped AgNPs in a suboxic matrix to explore
the effects of humic substances and S2– on AgNP. Initial findings suggest that the kinetics of humic-AgNP
interactions are rapid and that the PVP-capped AgNPs show minimal interaction with the sulphide or HA.
This contrasts with the behaviour of citrate-capped AgNPs where changes in particle size distributions
have been observed (Figure 1). Further investigations of these effects are in progress.
––– ––– ––– ––– ––– CaCl2 matrix 2–
Matrix + S Matrix + HA 2–
Matrix + HA + S Pure AgNP, no matrix Posters
Figure 1 Observed DLS size distributions for citrate-capped AgNPs in presence/absence of HA and S2–.
145
On the role of colloids and nanoparticles for the distribution of phosphorus in a forest
topsoil
Anna Missong1, Roland Bol1, Volker Nischwitz2, Sabine Willbold2, and Erwin Klumpp1
Institute of Bio- and Geosciences, Agrosphere (IBG-3)
1
2
Research Center Jülich, 52425 Jülich, Germany
E-mail: [email protected], [email protected], [email protected], [email protected]
Posters
Colloids and nanoparticles play an important role for the binding, transport and distribution of nutrients
like phosphorus in soil. High percentage of total phosphorus contents are associated to inorganic and
organic fine colloids < 450 nm but their relevance is often neglected within this soil fraction. In forest soil,
P is accumulated in surface and upper mineral layers but the lateral distribution of P in topsoil is highly
inhomogeneous.
In this study samples from a coniferous forest were taken along a 2 m x 0.5 m grid with 30% slope. The
effect of the slope position on the phosphorus distribution in the acidic topsoil samples was investigated.
Water dispersible colloids (WDC), which represent the transportable colloid fraction, were extracted from
field moist soil samples. Different size ranges (≤ 1µm, ≤ 450 nm, ≤ 100 nm) of WDC were separated and
analyzed. The Field Flow Fractionation technique coupled online to UV-, DLS- detector and inductively coupled plasma mass spectrometry (ICP-MS) enabled a size resolved characterization of the colloidal fraction
< 450 nm and their elemental composition (Fe, Al, P, Ca, Mn).
Colloids of surface- and mineral soil layers differed in colloidal composition and size distribution. Both
layers show differences regarding particle bound phosphorus concentrations between the size range of
100 and 450 nm. The total phosphorus content does not correlate with slope whereby the colloidal bound
phosphorus content increases with it.
The results confirm that P associated to colloids can be laterally translocated in soil and might be responsible for the heterogeneous distribution of P in the topsoil layers. Differences in size-dependent phosphorus
amounts indicate a preferential association of P to distinct colloid forms. To characterize the organic P
species liquid 31P-NMR measurements will be performed.
146
Interaction of polyacrylamide flocculants and acrylamide with clays, soil and sediments
I.Mnif1, C.Hurel1, A.G. Guezennec2, N.Marmier1
1 University of Nice Sophia Antipolis, Ecomers, 28 avenue Valrose, 06108 Nice cedex 2, France
2 BRGM, 3 Avenue Claude-Guillemin, BP 36009, 45060 Orléans Cedex 2, France
[email protected]
Polyacrylamide flocculants are used in numerous fields, particularly for water treatment and offshore
oil production. These polyacrylamide polymers, with an ultra-high molecular weight, are produced from
acrylamide monomer, which is known to be an animal and a suspected human carcinogen. The fate and
transport of acrylamide and polyacrylamide flocculants in the environment in the above contexts have
never been studied yet. In this study, we were interested in acrylamide and 2 anionic polyacrylamides of
different molecular weight: the first one is used as flocculent in an aggregates quarry, and the second one
is used in offshore oil extraction. For both acrylamide and polyacrylamides, batch experiments (sorption
isotherms) according to the protocol developed by the Environmental Protection Agency (EPA) [1] were
conducted on mineral soil phases, soil materials and sediments to determine the partition coefficient between the solid and the liquid phase (Kd), and to provide a better understanding of these molecules fate
when they are in contact with natural solid phases. For acrylamide and the polyacrylamide used in the
aggregates quarry, the tests were performed in freshwater with clays and sludge from one quarry site. For
polyacrylamide used in petrochemical, experiments were carried out in sea water with clays and marine
sediments.
Figure 1 presents the adsorption isotherms obtained for acrylamide in contact with kaolinite, illite and a
sluge collected in the quarry. The results from figure 1 indicate a weak affinity of acrylamide to clays and
to soil samples (Kd < 0.9 ml/g). These results are consistent with those of Arrowood (2007) [2] who found
low adsorption percentages (0-2.4%) of acrylamide on three soil types. This low affinity can be explained
by the high solubility and hydrophilicity of acrylamide, its small size and the negative charges of both acrylamide and the surfaces of solids tested, as shown by zeta potential analyzes. Acrylamide is mobile in the
soil since it cannot be trapped by mineral particles. Unlike the acrylamide, the two polyacrylamides tested
showed a strong affinity to clays, sludge and sediments.
Figure 1 Adsorption isotherms of acrylamide
onto two clays (Kaolinite, Illite) and sludge
from the aggregates quarry, with solid/liquid
ratio= 200 g/L, I= 10-3mol.L-1 at pH=7.0
Posters
References
1. W. R. Roy, I.Gkrapac, S.F.J. Chou, R.A. Griffin. Technical Ressource Document 1991, EPA/530-SW-87-006-F
2. T. J. Arrowood. PhD Thesis, University of Nevada 2007.
147
Synthesis and characterization of magnetite/clay composites
Musabekov K.B., Korzhynbayeva K.B., Tazhibayeva S.M., Dekany I., Zhanadilov O.Ye.
Al-Farabi Kazakh National University
Posters
Nowadays, the receipt and investigation of different properties of magnetite/clay composites is one of
the most rapidly developing areas of modern nanoscience. Magnetic materials known to mankind for a
long period, and it is well known, what kond of the role played by the magnetic phenomena in human life.
However, searching for data on the preparation and characteristics of magnetic composites showed that
these composites is very little studied. In connection with this research objective was synthesis of magnetite/montmorillonite and magnetite/kaolinite composites and study their different properties.
In this work were synthesized magnetite/montmorillonite and magnetite/kaolinite composites of sequential treatment with salts of iron (II) and (III).
Magnetic properties and phase analysis of these composites were characterized by vibration sample magnetometry and XRD analysis. Vibration sample magnetometry results were showed themselves above the
clay minerals have magnetic properties in native form, a fact confirmed by the absence of a magnetic hysteresis for them. The resulting composites are shown based on their magnetic properties and responsive
to an applied magnetic field. Depending on the availability of iron oxide particles in the inter-packet space
of montmorillonite and kaolinite minerals has the phenomenon of magnetic hysteresis. As the concentration of magnetite in the composites magnetization increases to a maximum value (27.6 emu/g and 31.6
emu/g), typical for magnetite/montmorillonite and magnetite/kaolinite composites, respectively. Magnetization values of the magnetite/montmorillonite and magnetite/kaolinite composites are comparable
with the magnetization value of magnetite, which is associated with the state of nanoscale magnetite
particles in the composite structure of clays.
Were synthesized magnetite/montmorillonite and magnetite/kaolinite composites, and with the inclusion of particles of magnetite in the structure of these minerals is proved by XRD and SEM. The results of these methods was also demonstrated the presence of magnetite phase in all the samples.
Based on these results it is concluded that synthesizing magnetite/montmorillonite and magnetite/kaolinite composites can achieve high rates of their magnetic properties. The concentration of magnetite in the
composites will be relatively is low.
148
Interaction of Some Peticides with Iron Organometallic Compounds
A. Boucif*, O. Hamrani*, N. Sabba**, Z. Hank* and S. Boutamine*
*Université des Sciences et de la Technologie Houari Boumediene (USTHB), Faculté de Chimie, Laboratoire d’Electrochimie, Corrosion,
Métallurgie et Chimie Minérale, BP 32, El Alia, Bab-Ezzouar,16111, Algiers Algeria. [email protected], [email protected]
**Université des Sciences et de la Technologie Houari Boumediene (USTHB), , BP 32, El Alia, Bab-Ezzouar,16111, Algiers Algeria
Laboratoire d’Hydrometallurgy and Inorganic Chemical Molecular, [email protected]
Particular chemicals like pesticides which use, in agriculture, became inescapable are engendering an environmental pollution and more particularly that of soils.
operate everything to reduce and control these pollutants. Some conventional adsorbing product such
carbon F400 are frequently used.
The adsorption on the synthetized metal organic complexes may be a alternate technique to disinfect
soils and waters polluted by pesticides and other chemicals.
In this context, some coordination compouds of iron were tested in the adsorption of mitrobuzin present
in contaminated water. The retained organic molecules are natural products (flavonoids).
The preliminary results seems encouraging and we report them here.
Retention of ionic pesticides at the soil–solution interface
Alba Otero1, Dora Gondar1, Sarah Fiol1, Juan Antelo2, Florencio Arce1
Department of Physical Chemistry and 2Department of Soil Science and Agricultural Chemistry, University of Santiago de Compostela,
1
15782 Santiago de Compostela, Spain.
The objective of this study is to obtain information of the adsorption process of pesticides in soils in order to be able to predict and control its fate in the environment. The retention of ionic pesticides paraquat and MCPA
by different soils (peat soil, forrest soil and vineyard soil)
has been analyzed. This retention capacity of the soils can
be interpreted as a function of some factors such as pH, ionic strength or the organic matter content. The results will
confirm that the organic and the mineral fraction of soils
can contribute differently to the behavior of pesticides in
soils and depending on the dominant phase experimental
adsorption data can be normalized for the organic carbon content (see figure).
149
Posters
Soil constitutes are an organized system that comprises different organic and mineral components. Its surface acts as a complex geochemical interface that establishes a boundary between soil and soil solution.
Pesticides are a class of persistent organic pollutants that play an important role in crop production and
protection. Among pesticides, we can find compounds with a big variety of chemical formulations that
can have adverse effects on human health and persist in the environment due to its high affinity for soil
organic matter, especially for humic substances. This affinity will be affected by the nature of the organic
matter and by the type of pesticide and will affect itself the transport, bioavailability and persistence of
these substances in the environment (Roldán et al., 2011, Anal Chim Acta, 699, 87–95).
Adsorption of Anionic Surfactant on Silica
Pengxiang Li1, Munehide Ishiguro2
1. Graduate School of Agriculture, Hokkaido University, [email protected]. 2. Research Faculty of Agriculture, Hokkaido University,
[email protected]
Introduction: Surfactants are widely used in many fields which are closely related to our life and environment. Large amount of studies were reported during the past several decades about the adsorption of cationic surfactant on silica and anionic polymers, when it comes to anionic surfactant on silica, there is only
few researches upon it, in this research, sodium dodecyl sulfate (SDS) adsorption on silica was investigated
under different pH (3, 5 and 7) and NaCl concentration (0.1, 100mmol/L).
Materials and Methods: Quartz silica of 1.2 μm in average diameter was purchased from Sigma-Aldrich.
SDS with linear alkyl chain was used. A batch method was taken to obtain the adsorption amount of surfactants. Surfactant concentration was measured by surfactant selective membrane electrode method.
Adsorption isotherms were fitted with both Langmuir and Frumkin–Fowler–Guggenheim (FFG) equation.
Result and Discussion: In 0.1mmol/L NaCl solution, whatever pH performed, the concentration of surfactant after equilibrium kept, infinitesimal changes happened, no binding was found. At lower NaCl concentration, SDS adsorption can hardly happen because the screening effect of Na+ decreased and the electric
repulsive force became larger.
In 100mmol/L NaCl solution, as the figure shows, a sharp increase as the first stage of adsorption isotherm
was observed. The slope of adsorption isotherms showed larger than unit in double logarithmic scale.
When the slope is unit, it is the so called “Henry slope”, which indicates the adsorption on isolated “equal
energy” site that follows the ideal adsorption of the Langmuir equation. The steeper slope indicated a
cooperative adsorption which was caused by the hydrophobic interaction among the adsorbed SDS ions.
SDS adsorption became stronger by gathering together, FFG equation was better fitted. The second stage
showed a Langmuir-increase and a pseudo plateau formatted when it was the third stage.
The adsorption at lower pH was larger than that at higher pH because the negative charge of the silica
increased with increasing pH and the increase of the negative charge induced the increase of repulsive
force between SDS and the silica.
Figure 1 Adsorption isotherms of
different pH and NaCl concentration
Posters
conditions
150
Adsorption characteristics of anionic surfactant and anionic dye onto alpha alumina
with small surface area
Tien Duc Pham*, Motoyoshi Kobayashi, Yasuhisa Adachi
Graduate School of Life and Environmental Sciences, University of Tsukuba,
Tennodai 1-1-1, Tsukuba-shi, Ibaraki 305-8572, Japan
[email protected]
We investigated adsorption of anionic surfactant sodium dodecyl sulfate (SDS) and anionic dye new coccine (NC) onto α-Al2O3 with low surface area as a function of pH and NaCl concentration. Figure 1 shows
that the SDS adsorption isotherms () onto α-Al2O3 as a function of NaCl concentration at pH 4 has a common
intersection point (CIP) corresponding to surface charge neutralization [1]. The CIPs were also observed at
pH 5 and pH 6. The SDS adsorption decreases with increasing electrolyte concentrations below CIP. Nevertheless, above CIP the salt effect is reversed so that the adsorption density reduces at lower ionic strength. In
Figure 2, the adsorption isotherms of new coccine () onto α-Al2O3 at pH 4 are indicated as a function of NaCl
concentration. The increase in the ionic strength decreases the maximum dye adsorption density. The trend
is different with surfactant adsorption. Furthermore, the maximum adsorption of both SDS and NC onto
α-Al2O3 increases with decreasing pH (data is not shown) because of the increase in positive surface charge.
While the change in pH upon SDS adsorption onto α-Al2O3 was observed, this change was not significant for
NC adsorption.
The calculated curves from 2-step adsorption model can reasonably represent experimental results of SDS
and NC adsorption isotherms onto α-Al2O3 at different salt concentrations (solid lines in Figure 1 and 2),
suggesting that the adsorption of SDS and NC onto α-Al2O3 should be described by a multilayer adsorption
than monolayer adsorption isotherms [2]. The maximum SDS adsorption density was much higher than NC
adsorption density, demonstrating the presence of hemimicelles or admicelles in the surfactant adsorption.
Figure 2 Adsorption isotherms of NC onto α-Al2O3
as a function of NaCl concentration at pH 4.
as a function of NaCl concentration at pH 4.
Posters
Figure 1 Adsorption isotherms of SDS onto α-Al2O3
References
1. T.P. Goloub, L.K. Koopal, B.H. Bijsterbosch, M.P. Sidorova, Langmuir 12 (1996) 3188.
2. J. Wang, C.P. Huang, H.E. Allen, D.K. Cha, D.-W. Kim, J. Colloid Interface Sci. 208 (1998) 518.
151
Performance of ionic MOFs on the capture of radionucleides
PRELOT Benedicte1, GENESTE Amine1, RIVES Sébastien1, NOUAR Farid2, FABRY Paul2, DEVIC Thomas2,
HORCAJADA Patricia2, YOT Pascal1, ZAJAC Jerzy1, SALLES Fabrice1
1
2
Institut Lavoisier UMR 8180 CNRS-Université Versailles Saint Quentin en Yvelines, 78035 Versailles France
E-mail :[email protected]
Recently, some crystalline hybrid porous solids known as Metal Organic Frameworks (MOFs) emerged as
promising systems for gas adsorption and drug encapsulation.1 Indeed these hybrid solids, constituted
by inorganic nodes (metal chains or clusters) linked each other by organic linkers, present a large specific
surface area and pore volumes as well as a high chemical versatility allowing to modulate the chemical and
physical properties indefinitely.
Even if few results are available in the literature, the adsorption by such solids possessing extra-framework
ions could be evidenced as a plausible, economic and simple solution to eliminate toxic contaminants in
water.2 Various parameters can influence the ability for sorption of porous solids such as the charge of the
framework, the adsorption interaction and the diffusion in the pores.3
For this study, we have followed a strategy combining experimental techniques (adsorption calorimetry
and isotherm, X-ray Diffraction) with computational approach (Molecular Dynamics) to elucidate both
the microscopic mechanisms in parallel of the macroscopic behavior allowing us to rationalize the ion
exchange process for both I- anion and Sr2+ cation in MOFs containing extra-framework ions. Further, one
anionic and one cationic MOF have been chosen for this study, in which the impact of the topology and the
framework charge is discussed on the ionic exchange properties, i.e. the adsorbed ion quantity as well as
the adsorption energy. We have clearly evidenced the high adsorption capacity of the materials studied.
This allows the potential use of such innovative materials for decontamination process to be envisaged.
References
1. G. Férey, Chem. Soc. Rev., 2008, 37, 191
2. (a) A. Sachse, A. Merceille, Y. Barrès, A. Grandjean, F. Fajula, A. Galarneau, Micro Meso Mater., 2012, 164, 251, (b) C. Delchet, A.
Posters
Tokarev, X. Dumail et al., RSC Adv., 2012, 2, 5707, (c) S. Sen Gupta, K.G. Bhattacharyya, Phys. Chem. Chem. Phys., 2012, 14, 6698
152
Dye adsorption at the TiO2/water interface and correlation with photocatalytic
degradation
DARMOGRAI Ganna1, KUS Monika2, MARTIN-GASSIN Gaelle 1, CAVALIERE Sara1, MEYNEN Vera 2, PRELOT
Benedicte1, ZAJAC Jerzy1
1
2Laboratory of Adsorption and Catalysis, Department of Chemistry, University of Antwerpen, Campus Drie Eiken, Universiteitsplein
1, B-2610 Wilrijk, Belgium
In numerous studies of photocatalytic degradation of organic pollutants, the main emphasis is usually
placed on the modification and fine-tuning of the catalyst surface properties to improve their photocatalytic efficiency under UV or Visible radiation. Much less attention is paid to the pollutant adsorption
stage, which is a pre-requisite for the ultimate photocatalytic reactions. Such characteristics of the adsorbed pollutant species as the strength and reversibility of their adsorption on the catalyst surface or their
orientation and concentration within the interfacial region may certainly affect the performance of the
photocatalytic process. There is thus an urgent need for systematic studies of the underlying adsorption
mechanisms.
The main interest of the present preliminary study was to establish the relationship between the dye
adsorption capacity of several powdered TiO2 samples, varying in particle size and morphology, and their
efficiency in photocatalytic dye degradation from aqueous solutions. For this purpose, Rhodamine 6G
was adsorbed from aqueous solution under various dye concentration, pH, and ionic strength conditions.
The following TiO2 samples were used as solid adsorbents (the crystalline composition, as determined
based on XRD measurements, is given in brackets): nanocrystalline anatase (100% anatase), P-25 Degussa
(80% anatase, 20% rutile), nanofibers synthesized using electrospinning method (68-75% anatase, 32-25%
rutile), as well as a series H nanotubes containing as-made, freshly calcined or calcined and aged samples. These materials were characterised by nitrogen gas adsorption and electrophoretic measurements
to know their specific surface area and surface density of electric charge under different experimental
conditions. Then the adsorption isotherms for Rhodamine 6G from aqueous solutions were determined
by means of solution depletion technique. Finally, the photobleaching and photocatalytic performance of
the TiO2 samples was tested under free pH and ionic strength conditions. The first conclusions drawn from
this work should certainly be useful in view of further optimisation of the overall photocatalytic treatment
for organic pollutant degradation.
Posters
153
Analysis of surface of the titanium electrode after precipitation of indium
Burkitbayevaa B.D., Argimbaevaa A.M., Rakhymbaya G.S., Dzhumanova
Nauryzbayeva M.K.
a
a
R.Zh., Kurbatova A.P.,
Al-Farabi Kazakh National University, Department of Chemistry and Chemical Technology
Abstract: Electrochemical characteristics of deposition and dissolution of indium in chloride solutions
using the method of cyclic voltammetry were determined. The effect of the polarization of the interval
and scan rate at electrochemical reactions which occur in the system was studied. Electron microscopy
observations and X-ray diffraction patterns confirmed the formation of crystalline indium deposits.
Posters
Keywords: indium, discharge-ionization, current density, scan rate, electrode process, potential
Currently, there is increasing interest to the problem of obtaining high-purity indium /1/. This work is a
continuation of studies of electrochemical behavior of In3+ on platinum and titanium electrodes to find effective ways of cleaning rough indium /2/. Methods of scanning electron microscopy and X-ray diffraction
analysis used in this work have revealed the presence of cathodic precipitated metallic indium on the surface of the titanium electrode and helped to find optimal conditions of the processes studied. Chronoamperograms of studies carried out were obtained to study the effect of electrolyte concentration, potential
and electrolysis time on the precipitation and dissolution of indium. Variation of potentials interval revealed the potential of total precipitation of indium on the surface of titanium electrode, which amounted to
-1.1 V. This result was obtained on the basis of X-ray diffraction analysis and scanning electron microscopy
of surface of samples of titanium electrode coated with metallic indium. Changing the concentration of
indium in the solution has a strong influence on the rate of recovery of indium. Analysis of the electrode
surface after polarization at different concentrations of indium in the solution (0.1 M) revealed an optimal
concentration of 0.5 M, when there is a maximum recovery rate of indium. Furthermore, the results of
scanning electron microscopy showed that the best precipitation for all three concentrations occurs at
the potential of -1.1 V. During the electrolysis of 0.5 M sodium chloride solution, indium (Ee = -1.1 V), the
formation of coarse sediments of indium on titanium surface is observed. Carrying out the electrolysis at
potentials of -0.8 V and -1.3 V results in the formation of non-uniform precipitation of amorphous indium.
Apparently at -0.8 V only beginning of precipitation of indium is observed, and at -1.3 V the recovery of
hydrogen occurs, complicating the process of precipitation of indium. Indium precipitations obtained in
these experiments were analyzed by XRD method.
Experiments on the effect of electrolysis time were carried out for a detailed investigation of indium precipitation process on the surface of titanium. The amount of precipitated indium and crystals become larger
with the increase of electrolysis time.
Chronoamperograms of indium precipitation and dissolution at potentials of E = -1.1 V for the cathodic
process and E = -0.5 V and E = 0.2 V for the anode were obtained to identify the potential of indium ionization on titanium electrode surface. It is obvious from the results of X-ray diffraction analysis and scanning
electron microscopy that the shift of dissolution potential in the anodic region leads to an increase in the
rate of oxidation of indium.
Thus the results of presented work can be used in the development of electrochemical method of indium
refining.
References
1. Yonghwa Chung, Chi-Woo Lee Electrochemical behaviors of Indium // Journal of Electrochemical Science and Technology. –
2012. - Vol. 3. – No. 1 – P/ 1-13
2. Burkitbaeva B.D., Argimbayeva A.M., Rakhymbay G.S., Dzhumanova R.Zh., Tuhmetova D.B. Electrochemical behavior of Indium
in sulfate solution // Bulletin Al-Farabi KazNU. Сhemical series. – Almaty, 2013. – №2 (70). – P. 102-106.
154
Potential of electrokinetic process for the remediation of estrogens in soil
Paula Guedes a, Eduardo P. Mateus a, Yadira Rodríguez a,b, Nazaré Couto a, Alexandra B. Ribeiro a,*
a
CENSE, Departamento de Ciências e Engenharia do Ambiente, Faculdade de Ciências e Tecnologia, Universidade Nova de Lisboa,
2829-516 Caparica, Portugal
b
Department of Chemical Engineering, University of Málaga, Campus de Teatinos, 29071 Málaga, Spain
*Corresponding author: [email protected], Tel.: +351 212948300, fax: +351 212948554.
Some organic contaminants can accumulate in organisms and cause irreversible damages in biological
systems through direct or indirect toxic effects. In this study, the feasibility of electrokinetic process (EK)
for the remediation of estrogens 17β-estradiol (E2) and 17α-ethynyl-estradiol (EE2) was studied in a stationary laboratory cell. Both compounds are defined as “emerging” contaminants and are known to be
endocrine disrupting agents.
Two soils were used in this study: S1 (Valadares, Vale de Milhaços, 0–15cm depth) and S2 (Paul de Magos,
Salvaterra de Magos, Portugal, 0–20 cm depth). Soil S1 (sandy) was used as a support medium and S2 (silty
loam) as the contaminated matrix. Four experiments were carried out without pH control at 0, 10 and 20
mA; and with pH control (anolyte, pH > 13) at 10 mA.
The analysis of the soil section near the anode and cathode end for all experiments showed that all the
contaminants were remediated during the experiment although at different extents. Electroosmotic flow
towards the cathode end was the mechanism responsible for the contaminants mobilization, being more
expressive when pH was controlled. Estrogens presented slightly different behaviours during EK. When 10
mA were applied 39 % of E2 and 50 % of EE2 remained in S2. When 20 mA were applied the remediation
only 30 and 35 % of EE2 and E2, respectively remained in S2. Between 44 to 69 % of the compounds were
degraded mainly due to the formation of ·OH radicals.
Remediation of organic contaminants seems to be feasible through an integrated approach with different
remediation/removal mechanisms (EK transport, electro- and photodegradation).
The results here presented are of valuable knowledge for the remediation of organic contaminants using
the EK process.
Keywords: Electrokinetic remediation, electroosmotic flow, electrodegradation, estrogens, soil
Acknowledgements
Financial support was provided by FP7-PEOPLE-2010-IRSES-269289-ELECTROACROSS - Electrokinetics across disciplines and continents: an integrated approach to finding new strategies for sustainable development, PTDC/
ECM/111860/2009 - Electrokinetic treatment of sewage sludge and membrane concentrate: Phosphorus recovery
and dewatering. N. Couto acknowledges Fundação para a Ciência e a Tecnologia for Post-Doc fellowship (SFRH/
BPD/81122/2011).
Posters
155
Potential of salt marsh plants for the remediation of organic compounds
Nazaré Coutoa, Ana Rita Ferreirab, Paula Guedesa, Eduardo P. Mateus a, Alexandra B. Ribeiroa
a
CENSE, Departamento de Ciências e Engenharia do Ambiente, Faculdade de Ciências e Tecnologia, Universidade Nova de Lisboa,
2829-516 Caparica, Portugal
b
Departamento de Ciências e Engenharia do Ambiente, Faculdade de Ciências e Tecnologia, Universidade Nova de Lisboa, 2829-516
Caparica, Portugal
*Corresponding author: [email protected], Tel.: +351 212948300, fax: +351 212948554.
To assess the potential of Halimione portulacoides and Spartina maritima for the removal of caffeine
(Caff), 2-hydroxy-4- methoxybenzophenone (MBPH) and triclosan (TCS) from aquatic medium, a 10-day
experiment was carried out. At laboratory conditions, plants were exposed to 1 ppm of each contaminant
in sediment elutriate and in sediment soaked in elutriate. Sediment, water and plants (with same age and
size) were collected in Tejo River estuary, Portugal. Target contaminants were analyzed in liquid (solid phase extraction) and solid samples (ultrasonic extraction) and determined by gas chromatography coupled
with flame ionization detector. Chlorophylls and carotenoid contents were assessed and suggested no
significant deletory effects resulting from the 10-days exposure to these organic contaminants at this concentration. Preliminary results suggest that remediation was achieved by different removal mechanisms
including photodegration and biological mechanisms. Results will be presented and discussed in the scope
of the suitability for a field scale remediation set-up.
Keywords: salt marsh plants, caffeine, 2-hydroxy-4- methoxybenzophenone, triclosan, sediment elutriate
Acknowledgements
Financial support was provided by FP7-PEOPLE-2010-IRSES-269289-ELECTROACROSS - Electrokinetics across disciplines and continents: an integrated approach to finding new strategies for sustainable development, PTDC/
ECM/111860/2009 - Electrokinetic treatment of sewage sludge and membrane concentrate: Phosphorus recovery
and dewatering. N. Couto acknowledges Fundação para a Ciência e a Tecnologia for Post-Doc fellowship (SFRH/
Posters
BPD/81122/2011).
156
Effect of pH on adsorption of arsenic onto fly ash
Justyna Ulatowska, Izabela Polowczyk, Tomasz Kozlecki, Anna Bastrzyk, Ewelina Szczalba, Zygmunt
Sadowski*
Wroclaw University of Technology, Faculty of Chemistry, Division of Chemical Engineering, Norwida 4/6, 50-373 Wroclaw, Poland
[email protected], http://iic.pwr.wroc.pl/
Arsenic in natural waters represents a serious health hazard. The chemical and biological weathering provide arsenic species to groundwaters [1]. High arsenic concentrations have been reported recently from
Chile, Argentina, India, Bangladesh, China, Taiwan, USA, Canada, Hungary and Poland [2,3]. Drinking water
having arsenic beyond permissible limit is dangerous for people life. It causes skin, lung, bladder and kidney cancer as well as pigmentation changes, skin thickening, neurological disorders, loss of appetite and
nausea [4]. Adsorption is a method frequently used for the water purification with arsenic [3].
In the present study, fly ash is used as adsorbent for removal of arsenic(III) in aqueous solution. Fly ash
was obtained from burning brown coal and biomass from the power plant in Zgierz (Poland). The objective of this study was to compare arsenic(III) removal at natural pH (imposed by fly ash; pH 8.5) with the
arsenic(III) adsorption at high alkaline (pH 12.5). The effect of adsorbent dose, temperature and contact
time was investigated.
The maximum static uptakes of arsenic(III) by fly ash at natural and high alkaline pH were achieved for adsorbent-to-arsenic ratios of 20 g/L and was 14 mgAs(III)/gsorbent and 30 g/L and was 20 mgAs(III)/gsorbent, respectively. Adsorption data of arsenic(III) onto fly ash were analyzed using Langmuir and Freundlich models.
Thermodynamic parameters for the adsorption process were determined at 25 oC, 35 oC and 45 oC. The
calculated values showed that arsenic(III) adsorption (both at natural and high alkaline pH) is a spontaneous and endothermic process. The process kinetics was evaluated by pseudo-first, pseudo-second order
and parabolic diffusion models. Pseudo-second order model exhibited the highest correlation with experimental data (R2 = 0.999). These results shows that the fly ash could be considered as potential adsorbent
for removal of arsenic(III) ions in aqueous solution, at both natural and high alkaline pH.
References
1. Rivas L.B and Sadowski Z., Bacteria generation of liquid arsenic waste and the application of water-soluble polymers for arsenic
ions separation. Reviews in Environmental Science and Bio/Technology, (2014) in press.
2. Guo et al., Removal of arsenite from water by synthetic siderite: Behaviors and mechanisms. Journal of Hazardous Materials
(2011) 186: 1847-1854.
3. Mohan and Pittman, Arsenic removal from water/wastewater using adsorbents – A critical review. Journal of Hazardous Materials (2007) 142: 1-53.
4. Malana et al., Adsorption studies of arsenic on nano aluminium doped manganese copper ferrite polymer (MA, VA, AA) composite: Kinetics and mechanism. Chemical Engineering Journal (2011) 172: 721-727.
Posters
157
Removal of hypophosphite ions from water using ultrasound
Akitsu Hanazato, Toshio Sakai*
Department of Chemistry and Material Engineering, Faculty of Engineering,
Shinshu University,
4-17-1 Wakasato, Nagano 380-8553, Japan
Email: [email protected],
URL:http://www.shinshu-u.ac.jp/faculty/engineering/chair/chem005/Index_Eng.htm
Posters
Hypophosphite ion (H2PO2-) is well known as a reducing agent for electroless plating and as hydrogen donor in catalytic hydrogenation of organic molecules. On the other hand, the plating waste solution after
electroless plaiting contains excess metal ions, H2PO2- and ligands that would cause serious contamination
if not removed before discharge. Thus, many methods have been developed for removal, recovery and
recycling of metal ions, H2PO2- and ligands from the plating waste solution. For example, H2PO2- is removed
and recovered as calcium phosphate formed through the reaction of phosphite ions (HPO32-) and phosphate (PO43-) with calcium ions (Ca2+). This means that H2PO2- must be oxidized to form HPO32- and PO43- for
removal and recovery of H2PO2- from water. Fenton reaction is one of the routes for oxidation of H2PO2- to
form HPO32- and PO43-, in which hydroxyl radicals (∙OH) act as an oxidizing agent for H2PO2-. Then, in this
work, the ultrasound is applied for removal, recovery and recycling of H2PO2- from water because H2PO2should be oxidized by ∙OH generated from sonolysis of water (H2O → H∙ + ∙OH). In particular, we examined
the effect of sonication time, ultrasound frequency, temperature, and solution pH on the sonochemical
oxidation of H2PO2- and the resulting HPO32- and PO43-. We found that the amount of H2PO2- oxidized and
the resulting HPO32- and PO43- increased with longer sonication time and higher frequency of ultrasound.
On the other hand, temperature and solution pH did not affect the oxidation of H2PO2-. Furthermore, we
revealed that the oxidation of H2PO2- was enhanced with the addition of hydrogen peroxide (H2O2) water
and titanium dioxide (TiO2) powder. The oxidation of H2PO2- was also enhanced by introducing oxygen (O2)
gas into the hypophosphite solutions. Note here that the oxidation of H2PO2- was not observed in the absence of ultrasonication even if H2O2 water and TiO2 powder were added and O2 gas was introduced. This
indicates that the oxidation of H2PO2- and generation of HPO32- and PO43- were enhanced by combination
of ultrasonication with H2O2, TiO2 and O2.
158
Hydrodynamic behavior of Zero-valent Iron Permeable Reactive Barriers: Effects of
Permeability Loss
U. Santisukkasaem and D. B. Das
[email protected] [email protected] and [email protected]
Department of Chemical Engineering, Loughborough University, LE11 3TU, United Kingdom
The permeable reactive barrier (PRB) is a widely used technology for in-situ subsurface remediation as it is
capable of treating large contaminant plumes cost effectively. Zero-valent iron (ZVI) is a reactive material
that has been extensively used as it is highly reactive and suitable for treating various kinds of contaminants, i.e. hydrocarbons and heavy metals. Despite the facts that ZVI-PRB has been used in groundwater
remediation technologies, the complex mechanisms that occur in the treatment process need further
studies and the longevity of the system is unpredictable. The significant issues that need to be addressed
which is intimately related to the hydrodynamic of PRB is the rate of mineral precipitation and permeability/porosity reduction within the PRB as well as the potential of ZVI-PRBs for remediation of contaminants.
A series of column experiments has been set up (14 cm inner diameter and length of 90 cm) and operated
with the conditions imitating the natural groundwater environment, i.e. flow rate and water constituents.
The experimentally measured values of main parameters following Darcy’s law will be used in calculating
the permeability and computer simulation. The corroded ZVI will be analysed to identify the composition
of the precipitates and to determine the porosity changes using micro X-ray CT scanner (µCT) and X-ray
Diffraction (XRD). From the flow column experiment, it can be seen that there is a drop in flow rate and
a decrease in the intrinsic permeability relative to time, i.e. total flow. The XRD detected the chemical
components of Magenetite and Maghemite which are the iron oxides that occur from the reduction of
iron in water. The image from µCT indicated the changes in particle size, pore size and porosity. It can be
concluded that the pores have been blocked due to the mineral precipitation thus reducing the flow rate
and permeability. The results of the computer simulation can be used to determine the rate of mineral
precipitation and support in designing the appropriate PRB, i.e. in term of longevity.
Keywords: Zero-valent iron, permeable reactive barrier, hydrodynamic, mineral precipitation
Posters
159
Protein complexation with Humic acids
Wen-Feng Tan*, †, Yan Li†, Ming-Xia Wang †, Willem Norde †, and Luuk K. Koopal ‡
†
College of Resources and Environment, Huazhong Agricultural University, Wuhan, P. R. China.
‡
Laboratory of Physical Chemistry and Colloid Science, Wageningen University, Dreijenplein 6, 6703 HB Wageningen, the Netherlands
Humic substances (HS), including humic acids (HA) and fulvic acids (FA), are important components of soil
systems. The reaction between enzymes and soluble humic matter has been attributed to co-polymerisation, adsorption and encapsulation of enzymes into the inner structure of humic matter. The importance of
electrostatic and hydrophobic interactions between humic acids and proteins concluded that parameters
like mixing ratio of HA and protein, pH and ionic strength determined the extent of HA-protein complexation and aggregation of the complexes. Complexation of oppositely charged HS and protein is a form
of ‘complex coacervation’ or ‘associative phase separation’. HS form strong complexes with oppositely
charged proteins, which will lead to changes in the enzyme activity. The effect of soil HS on the activity
and stability of two enzymes was investigated as a function of pH, ionic strength and mass ratio HS/enzyme. Humic acid (JGHA) and fulvic acid (JGFA) are negatively charged, lysozyme is net positive at pH values
below 10.4 and urease is net positive below pH 5.2 or net negative above pH 5.2. The enzyme activities in
the HS-enzyme complexes were suppressed when the enzymes were oppositely charged to the HS. The
largest activity suppression was observed around the mass ratio HS/enzyme where the HS-protein complex was at its isoelectric point (IEP). At the IEP strong aggregation of the complexes led to encapsulation
of the enzyme. The ionic strength was important; an increase decreased complex formation, but increased
aggregation. Due to the larger hydrophobicity of JGHA than JGFA, the reduction in enzyme activity was
stronger for JGHA. The enzyme stability decreased also maximally at mass ratio around the IEP of the complex when HS and protein were oppositely charged. When urease and HS were both negatively charged
no complexes were formed, but the presence of JGHA or JGFA improved the activity and stability of the
enzyme.
References
1. Li Y, Tan WF, Koopal LK, Wang MX, Liu F, Norde W. Influence of soil humic and fulvic acid on the activity and stability of lysozyme
and urease. Environ Sci Technol, 2013, 47: 5050-5056.
2. Tan WF, Koopal LK, Norde W. Humic substance charge determination by titration with a flexible cationic polyelectrolyte. Geochim
Cosmochim Acta, 2011, 75: 5749-5761
3. Tan WF, Koopal LK, Norde W. Interaction between humic acid and lysozyme, studied by dynamic light scattering and isothermal
titration calorimetry. Environ Sci Technol, 2009, 43: 591-596.
4. Tan WF, Koopal LK, Weng LP, van Riemsdijk WH, Norde W. Humic acid protein complexation. Geochim Cosmochim Acta, 2008,
Posters
72: 2090-2099.
160
Biocomposites on the base of yeast cells and diatomite such as sorbents of metal ions
Tazhibayeva S.M., Korzhynbayeva K.B., Musabekov K.B., Zhubanova A.A., Burkitbaev M.M.
[email protected] and www.kaznu.kz
The problem of wastewater treatment is one of the most actual problems of modernity. Especially also
extremely actual problem is cleaning wastewater of metallurgical industries from the metal ions. Natural
minerals and synthetic ion-exchangers are widely used for remove the metal ions. Alternatively, they may
serve as microorganism cells containing on its surface a different of functional groups like amine, carboxyl,
hydroxyl, phosphate, sulfide, sulfhydryl, etc.
Were conducted experiments on the adsorption of ions Сu2+ and Pb2+ on the surface of yeast cells Rhodotorula glutinis. It has been shown that at the initial concentrations in the range of salts of Cu2+ and Pb2+ from
10-6 to 10-1 mol/l the removal degree of metal ions varies between (95.2 and 98.3)% to (50.1 and 59.7)%
for ions Cu2+ and Pb2+, respectively. In this case the adsorption equilibrium is reached after 30 minutes.
Method of IR spectroscopy shows that the interaction of yeast cells with ions Cu2+ and Pb2+ is realized by
amino-, phosphate, carboxylic and hydroxyl groups of the surface, the ions Cu2+ are dominant donor-acceptor interaction with amino groups and ions Pb2+ - ion exchange with the phosphate and carboxyl groups.
Due to the high lyophilic surface of cells their separation from solutions difficult. Therefore were carried
out experiments to immobilize the cells Rhodotorula glutinis on the surface of natural mineral diatomite.
Diatomite also has high sorption capacity with respect to the ions Cu2+ and Pb2+, but does not provide complete water treatment. The removal degree of Cu2+ and Pb2+ ions by diatomite in the concentration range
of their salts 10-5-10-1 mol/l is (92.1-15.6)% for Cu2+ ions and (95.6-20.3)% for Pb2+ ions.
Experiments to immobilization of Rhodotorula glutinis cells showed that the attachment of cells to solid
surfaces most efficiently at the surface of diatomite provisional modifications of polyethylenimine solution
with a concentration of 0.03 base-mol/l. Modification of mineral surface with cationic polymer creates
favorable conditions for attachment thereto of negatively charged cells of microorganisms. It is shown that
by using the obtained composite biosorbent to remove of Cu2+ and Pb2+ ions from solutions the treatment
degree of water is reaches 97.8-99.4 %.
Posters
161
Regulation of biodispersies stability by catonic polymers
Tazhibayeva S.M., Musabekov K.B., Eskeldinova Zh.K., Zhubanova A.A.
[email protected] and www.kaznu.kz
Posters
One of the factors limiting the widely use of cells of microorganisms in water treatment, is the difficulty
of separating them from solutions. To solve this problem can be used flocculation of biological dispersion
with polymers. Therefore we attempted to flocculation of yeast cells Sacharomyces cerevisae, algae and
spherosome Shlorella vulgaris and plant cells spherosome by using cationic polymers like polyethyleneimine (PEI) and polydimethyldiallylammonium chloride (PDMDAAH).
Suspension of yeast cells and spherosome is fairly stable, the value of their optical density only slightly changed over time. Introduction of the suspension of yeast cells Sacharomyces cerevisae and algae
Shlorella vulgaris solutions of PDMDAAH and PEI with concentration range 10-6-10-1 base-mol/l leads to a
substantial decrease in their optical density, and with increasing polymer concentration to increase the
settling rate of the particles. This is due to flocculation of biodispersions in result of adsorption on them
the polymer macromolecules.
Analysis of data on the aggregation of yeast cells, algae and spherosome of plant cells in the presence of
PEI and PDMDAAH, change their electrokinetic potential, PEI adsorption on the surface of yeast cells suggests that along with flocculation by neutralization mechanism in these systems occurs due to aggregation
on account of bridge formation. This is confirmed by experiments on the change of the reduced viscosity
of the cell-PEI.
Calculation of the interaction energy of cells in the presence of polymers is difficult because of the complexity into account the specific adsorption of polymer macromolecules. On the cell surface interaction
energy values Sacharomyces cerevisae cells in a medium of sodium chloride are high in a wide range of distances between the particles, the negative energy values are found only at distances greater than 6500Å.
From this it follows that the flocculation of yeast cells with cationic polymers proceeds by a mechanism for
further aggregation accompanied by the formation of the amorphous structure.
162
Decontamination of solution containing radioactive strontium by sodium nonatitante
Arnaud Villard, Guillaume Toquer, Bertrand Siboulet, Agnès Grandjean and Jean-François Dufrêche
Institut de Chimie Séparative de Marcoule (ICSM), UMR5257, UM2-CEA-CNRS-ENSCM, Site de Marcoule, BP 17171, 30207 Bagnols-sur-Cèze, France
After using a combustible in nuclear reactor, this latter contains different radioactive elements, which do
not represent an interest to produce energy. These elements are called fission products. One of them,
which have a long half-life, is the strontium 90 (90Sr). After the dissolution of the combustible in concentrated nitric acid, strontium is dispersed in an aqueous as a divalent ion Sr2+. Thus, in order to reduce the
volume of the wastes, strontium has to be concentrated, and the current dominant process is co-precipitation. However this process produces a lot of secondary wastes that need a special treatment. In order
to reduce these secondary wastes, different processes have been studied and an interesting one is solid-liquid extraction. Different kinds of inorganic material have been proposed as extractants of strontium and
one group emerges because it presents a high selectivity and a good radioactive stability: porous titanates.
Among these materials, sodium nonatitanate, of chemical formula Na4Ti9O20, xH2O, has a good cationic
exchange capacity [1] and it has been studied by several experimental and theoretical investigations.
As any oxide, the exchange capacity of sodium nonatitanate is function of the pH [2]. In order to minimize
the influence of the pH on the adsorption of the strontium by the sodium nonatitanate, sodium acetate
have been used as buffer. A solution containing strontium nitrate and sodium acetate has been used as a
simulant of nuclear solution in order to model the adsorption of the strontium [3]. We show that the exchange is governed by nearest neighbours interactions in the solid phase [4]. The acidic constant has also
been obtained thanks to the modelling of the adsorption rate as a function of the pH. Such general studies
provide important relevant information for the design of the practical applications.
References
1. S.F. Yates et al., Sodium nonatitanate: a highly selective inorganic ion exchanger for strontium, Sep. Sci. Tech., 36 (5-6), 867-883,
2001
2. A. Merceille et al., The sorption behaviour of synthetic sodium nonatitanate and zeolite A for removing radioactive strontium
from aqueous wastes, Sep. Pur. Tech., 96, 81-88, 2012
3. A. Merceille et al., Effect of the synthesis temperature of sodium nonatitanate on batch kinetics of strontium-ion adsorption
from aqueous solution, Adsorption, 17, 967-975, 2011
4. A. Villard et al., in preparation
Posters
163
One-step synthesis of δ-MnO2 nanoparticles using ascorbic acid and their scavenging
properties to Pb(II), Zn(II) and methylene blue
Ming-xia Wang†, Pai Pang†, Wen-Feng Tan†, Luuk K. Koopal‡, and Fan Liu†,*
†
College of Resources and Environment, Huazhong Agricultural University, Wuhan, P. R. China.
‡
Laboratory of Physical Chemistry and Colloid Science, Wageningen University, Dreijenplein 6, 6703 HB Wageningen, the Netherlands
Posters
As environmentally friendly materials, manganese dioxides with a layered structure (δ-MnO2) display good
adsorption properties to heavy metals (such as lead, zinc and copper) and dyes (such as methylene blue
(MB) and Congo red); the latter also undergo oxidative degradation. δ-MnO2 materials are usually prepared by redox reactions using a variety of methods that result in different surface areas, particle sizes and
types and numbers of structural defects of the synthesized δ-MnO2. At lower temperatures, the redox
reaction is easier to control, and the SSA of obtained δ-MnO2 is larger. Furthermore, the scavenging to
heavy metals of δ-MnO2 is much more superior.
Ascorbic acid (AA) as a strong organic reducing agent can reduce high-valence manganese efficiently under
mild conditions to produce δ-MnO2 with a large SSA. Under ice-water bath condition, at pH2 and pH3,
well-crystalline layered δ-MnO2 was formed (Figure 1). The SSAs of the S10-3 and S10-5 samples were 180 and
207 m2/g. Due to their large SSAs and tiny particle sizes, the reactivity of the samples with respect to metal
ion adsorption revealed pseudo adsorption capacities of 3425 mmol Pb2+/kg and 1789 mmol Zn2+/kg. After
120 min at room temperature, 97% of the MB was adsorbed, and approximately 68% was oxidized (Figure
2). The adsorbed amount and the level of oxidation increased with increasing temperature and decreased
with increasing pH.
Figure 1 XRD patterns of samples synthesized at a Figure 2 MB decolorization efficiency of the tested samKMnO4/AA of 10 and different pH values
164
ples at 25 °C over different reaction times
Effect of Soil Colloidal Properties on Surface Runoff from Tottori Masa Soil
Kenta YAMADA1, Motoyoshi KOBAYASHI1, Haruyuki FUJIMAKI2
Graduate School of Life and Environmental Sciences, University of Tsukuba,
1
1-1-1 Tennodai, Tsukuba, Ibaraki, 305-8572, Japan;
Arid Land Research Center, Tottori University, 1390 Hamasaka, Tottori, Tottori, 680-0001, Japan
2
[email protected]
We investigated the relationship between interfacial chemical properties of Tottori Masa soil and the surface runoff from the soil induced by raindrops generated with a compact rainfall simulator.
The zeta potential of the soil colloidal particles demonstrated that the soil has pH-dependent negative
charge; the absolute values of the zeta potential of the soil increase with increasing pH. The soil particles
flocculated when the magnitude of zeta potential was low and the salt concentration and the valence of
counter ions were high. These results suggest that flocculation-dispersion behavior of the soil follows the
DLVO theory [1].
Figures 1 and 2 show the effects of pH and counter ion type on the surface runoff from Tottori Masa soil.
The surface runoff increased with increasing pH, suggesting that the runoff was enhanced under dispersed
condition (Fig.1). This finding is in good agreement with the result of zeta potential. We consider that, at
dispersed state, detached particles produce surface crust with low hydraulic conductivity. While both 1
mM CaCl2 and 10 mM NaCl are in the rapid coagulation regime where the electric repulsion is negligible,
the runoff induced by 1 mM CaCl2 rainfall was less than that by 10 mM NaCl. This behavior cannot be explained by the DLVO theory. We consider that calcium ions provide an additional particle-particle binding
force [2] and thus reduce the surface runoff by inhibiting the formation of soil crust.
Figure 1 Effect of pH on runoff from Tottori masa soil. Figure 2 Effect of electrolyte on runoff from Tottori masa
Rainfall intensity was 71.5±6 mm/h (vertical bars de- soil. Rainfall intensity was 71.5±6 mm/h(vertical bars denote a standard derivation).
Posters
note a standard derivation).
References
1. Cosgrove, T., Colloid science: principles, methods and applications, 2010.
2. Kobayashi, M., Strength of natural soil flocs. Water Research, 2005. 39(14): pp. 3273-3278.
165
The Mechanism of degradation on 4-Chlorophenol by Pulse Radiolysis
Yinxin Gao1, XiLei Zhao1, Jing Wang2, Yu Zhang1*, Min Yang1
(1.State Key Laboratory of Environmental Aquatic Chemistry, Research Center for Eco-Environmental Sciences, Chinese Academy of
Sciences, POB 2871, Beijing 100085, CHINA; 2. Beijing Brunt Technology Co. Ltd, Beijing 100029, CHINA)
The aim of the reactions of ·OH radicals generated by radiolysis in N2O-purged aqueous solutions with
4-chlorophenol(4-CP) have been investigated, especially focusing on the addition to the aromatic rings
and the direct electron transfer of ·OH radicals. Using the pulse radiolysis technique, different absorption
spectral features of the short-lived transients which are produced by reaction with ·OH radicals at different
pHs and the their corresponding rate constants have been determined. The results showed that ·OH preferentially added to the aromatic ring forming 4-chlorodihydroxycyclohexadienyl radical, which had a strong
adsorption at 310nm, and it followedby the second-order reaction which the rate constant was measured in acid and neural condition, as 2.86×109L3mol-1s-1 and 4.1×109L3mol-1s-1, respectively. In addition, in
order to give good selective oxidation to get chlorinated phenoxyl radical, azideradical(·N3) and sulfate
radical(SO4-·) have been shown. The results suggested that the formation of 4-chlorophenoxyl radical was
attributed to direct electron transfer and dehydration of 4-chlorodihydroxycyclohexadienyl radical. And
the adsorption spectrums of this chlorinated phenoxyl radical should be at 350nm and 400nm. In neutral
aqueous solution, the 4-chlorodihydroxycyclohexadienyl radical was the dominant short-lived intermediate formed during the period of radiolysis of 4-chlorophenol.
Keywords: Mechanism of degradation; 4-Chlorophenol; Pulse Radiolysis; Rate Constants
Transport and retention of multi-walled carbon nanotubes in different porous media
Miaoyue Zhang, Daniela Kasel, Anne Berns, Harry Vereecken, Erwin Klumpp
Agrosphere Institute, IBG-3, Forschungszentrum Jülich GmbH, 52425 Jülich, Germany
Posters
The applications of multi-walled carbon nanotubes (MWCNT) will inevitably lead to their release into environment but little is known about the fate and behavior of MWCNT when exposed to environment. This
study deals with the transport and retention of MWCNT in different porous media (quartz sands, silty loam
and loamy sand) at different input MWCNT concentrations and low flow rates. MWCNT concentrations in
the effluent and in the porous media were determined for breakthrough curves and retention profiles. To
more accurately understand the fate of MWCNTs, the breakthrough and deposition data collected were
simulated by using HYDRUS-1D. In quartz sands, results demonstrate that normalized MWCNT transport
increased with higher input concentrations and in coarser textured sand. The retention profiles showed
that the majority of MWCNT retention occurred near the surface of the porous medium, especially for
lower input concentrations and smaller sand sizes. In undisturbed soils, results revealed almost complete retention of functionalized MWCNT. More than 86% of MWCNT were recovered in the soil profile at
conditions close to saturation. At lower water-saturation, MWCNT retention in the upper soil layers was
enhanced. The co-transport of the pesticide Chlordecone in different porous media will also be discussed
in this paper.
166
Direct Electrochemistry of Horseradish Peroxidase based on Carbonized Chicken
Eggshell Membranes Materials
Di Zhang1,2 He Zhao2* Yuping Li2 Hongbin Cao1,2
1 Beijing Engineering Research Center of Process Pollution Control, Beijing 100190, China
2 Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
* Corresponding author, Email: [email protected]
The eggshell membrane is a reliable and sustainable resource for clean energy storage as over 1000 billion
eggs are consumed per year globally. Nanoscale carbon electrode materials are synthesized by carbonizing
a daily available biowaste in the form of chicken eggshell membranes (CESM). The structure of modified
electrode was characterized by scanning electron microscopy (SEM), cyclic voltammetry (CV) and electrochemical impedance spectroscopy (EIS). The results showed it was a three-dimensional carbon film composed of interwoven connected carbon fibers (Fig. 1). Two obvious redox peaks and an excellent current
response (near±1mA ) was observed in PBS with a 3-electrode system (Fig. 2). Horseradish Peroxidase
(HRP) enzyme was easily immobilized onto the CESM modified glass carbon electrode (GCE). The unique
structure and highly electrical conductivity of the CESM material allows establishing very fast direct electron transfer and good biocompatibility between HRP and electrode, making it potentially attractive for
the application to biosensor and catalytic degradation.
1.0
0.8
0.6
(a) Bare GCE
(b) CESM-GCE
(c) HRP-CESM-GCE
Current (mA)
0.4
0.2
0.0
-0.2
-0.4
-0.6
-0.8
-1.0
-0.6
-0.4
-0.2
0.0
0.2
0.4
0.6
Potential (V vs. NHE)
Figure 1 SEM images of CESM-GCE in 50μm(A) and
Figure 2 Cyclic voltammograms of pH 7.0 PBS
in 5μm (B). The inset is the high-resolution image of
solution, obtained at (a) bare GCE electrode,
the selected area.
(b) CESM modified GCE electrode, (c) HRP immobilized CESM-GCE electrode.
Posters
167
Development of Functionalized Graphene Electrode for Water Softening
Trinh Ngoc Tuan1, Sangho Chung1, Jae Kwang Lee2, Jaeyoung Lee1, 2*
Electrochemical Reaction and Technology Laboratory (ERTL),
1
Ertl center for Electrochemistry and Catalysis,
2
Gwangju Institute of Science and Technology (GIST), Korea
*
Corresponding Author, email: [email protected]
The hardness in water represents the contents of divalent ions such as iron, manganese, copper especially,
magnesium and calcium. Conventional softening technologies including reverse osmosis (RO) and electrodialysis (ED) for hardness treatment have been developed. However, they still have several disadvantages
such as fouling of membrane and high operating cost. Of late, Capacitive Deionization (CDI) is attractive
technology for water desalination and softening by very low capacitive current of electrochemical double
layer. Among various carbon-based materials used for electrode fabrication, graphene (rGO) has been
intensively studied due to its excellent electrical conductivity and high surface area. However, graphene
difficultly disperses in water because of its strong Van-der-Vaals force and hydrophobicity, as well as low
capacitance causing limitation in making CDI electrode. In this work, we successfully prepared uniformly-dispersed rGO in aqueous solution through control reduction process of graphite oxide and hence enhance ion adsorption ability of in CDI cell system. Additionally, graphene also is composited and activated
by MnO2 in Alkaline condition at high temperature hence, enhance considerable surface area, specific
capacitance by MnO2 presentation as well as improve CDI performance. The effect of parameters to CDI
process is investigated in order to optimize the softening efficiency. The voltage of 1.5 V is chose to supply
power for this system and maximum ion removals gained can be comparable to other researches.
Posters
Keywords: Capacitive Deionization, Graphene, MnO2, Applied voltage, Flow rate.
168
Enhanced energy generation with capacitive electrodes driven by Exoelectrogengenerated ionic currents
Marta C. Hatzell,1 Roland D. Cusick,2 & Bruce E. Logan3
Department of Mechanical Engineering, Penn State University, USA; [email protected]
1
Department of Civil & Environmental Engineering, University of Illinois-Urbana Champaign, USA; [email protected]
2
Department of Civil & Environmental Engineering, Penn State University, USA; [email protected]
3
Bioelectrochemical systems (BESs) have the potential to generate electricity through coupling wastewater
organics oxidation by bacteria, to a cathodic reaction such as oxygen reduction. Power production from
BESs has improved over the last decade, yet still remains on the order of 1-2 W m-2 (cathode). The recent
synergy between salinity gradient energy technologies (e.g. reverse electrodialysis (RED)) and microbial
fuel cells was shown to significantly boost the power from BESs by nearly 5 times [1, 2]. Yet RED currently
requires a large number of ion exchange membranes, which results in high cost.
Capacitive mixing (CapMix) is an emerging salinity gradient energy technology which harvests energy
through the controlled transfer of ions to and from capacitive electrodes in river and seawater solutions
[3, 4]
. CapMix has suffered from low power densities, but is still promising because materials cost are low.
Experiments were conducted to evaluate the potential synergy between BESs and CapMix (Fig 1a). Results
indicated that the presence of the BES electric field improved the charging rate of the capacitive electrodes. This resulted in an increase in the energy harvested from the CapMix process with synthetic river and
seawater solutions by 60 times from 0.04±0.003 mJ cycle-1 (without BES) to 2.64±0.240 mJ cycle-1 (with
BES)[5] (Fig 1b). Furthermore, the electric field induced charging mechanism, may have implications for
enhancing desalination rates in membrane based capacitive deionization systems.
b)
Figure 1 (a) Capacitive mixing – Bioelectrochemical system schematic and (b) energy extracted from the
combined systems as a result of different BES operating conditions.
References
1. Cusick, R.D., Y. Kim, and B.E. Logan, Science, 2012, 335, 1474-1477.
2. Kim, Y. and B.E. Logan, PNAS, 2011, 108, 16176-16181.
3. Brogioli, D., Physical Review Letters, 2009, 103, 058501.
4. Brogioli, D., R. Zhao, and P.M. Biesheuvel, Energy & Environmental Science, 2011, 4, 772-777.
5. Hatzell, M.C., R.D. Cusick, and B. Logan, Energy & Environmental Science, 2014, DOI: 10.1039/c1033ee43823f.
169
Posters
a)
Solid-State NMR Studies on Adsorption of Electrolyte Ions in Carbon Materials with
well-defined Porosity
Martin Oschatz,a) Lars Borchardt,a) Felix Hippauf,a) Silvia Paasch,b) Eike Brunner,b) Stefan Kaskel a)
a)
Department of Inorganic Chemistry, Dresden University of Technology, Bergstraße 66, D-01069 Dresden, Germany
b)
Department of Bioanalytic Chemistry, Dresden University of Technology, Bergstraße 66, D-01069 Dresden, Germany
The demand for renewable energy sources and advanced energy storage devices steadily increase in this
century of dwindling fossil fuel resources. Among them, electrochemical double-layer capacitors (EDLCs) stand out due to their high power densities and nearly unlimited cycle life [1]. Due to their chemical
inertness, high electric conductivity, and large specific surface area, porous carbon materials are used in
most EDLCs. Further tuning of their structure and a better understanding of the relationship between
their properties and the EDLC performance is highly desired. Recently, Chmiola et al. found that there
is a capacitance increase when the pore size of the carbon materials becomes lower than the critical
solvent shell size and the formation of a double-layer would not be possible from the theoretical point
of view [2]. These findings forced the development of novel microporous carbon materials for the use in
EDLCs as well as the use of new techniques for the characterization of the carbon-electrolyte interaction.
Next to small-angle neutron scattering and theoretical simulations especially nuclear magnetic resonance
spectroscopy (NMR) was found to be a useful method for the investigation of the ion adsorption in microporous carbons [3-4].
In the present contribution a series of porous carbon with well-defined pore sizes ranging from 0.6 nm
to 4.5 nm is used for solid-state NMR investigations on the adsorption of Tetraethylammonium-tetrafluoroborate (TEABF4) ions (1M solution in acetonitrile). Our investigations focus on ordered mesoporous
carbide-derived carbons (OM-CDCs), mesoporous CMK-3, and microporous CDCs. Materials are loaded
with the electrolyte solution or the pure solvent for comparison. Magic angle spinning (MAS) 1H, 11B, and
13
C NMR measurements show that the chemical shift of NMR active nuclei located at molecules adsorbed
in porous carbon materials of comparable degree of sp2 hybridization is strongly correlated with the pore
size [5]. However, the characteristic diamagnetic shift is clearly influenced by the hybridization state of
the carbon atoms. In carbon materials with sufficiently large pores, electrolyte molecules tend to reside
closer to the pore walls than the solvent molecules (AN) which are to some extent “screened” from the
influence of the pore walls by the electrolyte. Removal of the solvent by evacuation results in a removal of
the solvent shell and brings the electrolyte molecules into closer contact with the pore wall. If adsorbed in
pores <1 nm diameter, solvent removal does not result in a further increase of the diamagnetic shift. This
supports the idea that the electrolyte molecules do not exhibit an intact solvent shell in such small pores.
References
Posters
1. P. Simon, Y. Gogotsi, Nat. Mater., 2008, 7, 845.
2. J. Chmiola, G. Yushin, Y. Gogotsi, C. Portet, P. Simon, P. L. Taberna, Science, 2006, 313, 1760.
3. S. Boukhalfa, L. He, Y. B. Melnichenko, G. Yushin, Angew. Chem., Int. Ed., 2013, 52, 4618.
4. A. C. Forse, J. M. Griffin, H. Wang, N. M. Trease, V. Presser, Y. Gogotsi, P. Simon, C. P. Grey, Phys. Chem. Chem. Phys., 2013, 15,
7722.
5. L. Borchardt, M. Oschatz, S. Paasch, S. Kaskel, E. Brunner, Phys. Chem. Chem. Phys., 2013, 15, 15177.
170
Temperature and size effects on the desalination of water
Mathijs Janssen, Andreas Härtel, and René van Roij
Institute for Theoretical Physics, Utrecht University
Leuvenlaan 4, MG 305
3584 CE Utrecht
The Netherlands
Phone: +31 30 253 2955
E-mail: [email protected] / [email protected] / [email protected]
We investigate the effect, which either varying the temperature or the pore and engine sizes have on the
properties of blue engine and desalination cycles. Desalination cycles were found to be most effective
when a huge bath of cold water is used. There is a ~10% decrease in required energy when changing from
equatorial to arctic sea water and another ~10% decrease when changing the volume of the desalination
bath from the volume of the engine to a 10x larger one.
Furthermore, we studied the effect of using water at different temperatures and electrodes build from
pores of different sizes within one cycle. Saline water reservoirs at different temperatures can be obtained
by e.g. pumping sea water from depths to the surface or by using cooling water from industrial facilities
in an intelligent way. Desalination becomes increasingly cheap when performing the charging step in sea
water of lower temperature than the discharging step. Interestingly, the characteristics of the engine (pore
size, pore volume, bath volume) can be tailored such that the required energy vanishes already for small
temperature differences.
These positive temperature and size effects on the efficiency are not at all exclusive to desalination cycles;
similar effects are also observed in blue energy cycles. We find that blue energy harvesting can be enhanced when fresh water is used which has a higher temperature than the sea water. For large temperature
differences of the order of 50 degrees this boosts the work per cycle by a factor of two, compared to existing techniques (see figure).
Posters
Figure Blue energy cycle in the potential – charge representation. Stroked lines represent the upper part of the cycle,
connected to fresh water reservoirs of different temperature.
References
1. D. Brogioli, Phys. Rev. Lett. 103, 058501 (2009)
171
Preparation of Chestnut-like Carbon Electrodes for Capacitive Deionization
Seon Ho Leea,b, Won Keun Sond, Kyung Suk Kangd, Dong-Hyun Pecka, Sang-kyung Kimb,c, Doo-Hwan Jungb,c*
a
Department of Chemical and Biomolecular Engineering, Yonsei University, Seoul, 120-749, Republic of Korea
b
Fuel Cell Research Center, Korea Institute of Energy Research (KIER), Daejeon, 305-343, Republic of Korea
c
Advanced Energy Technology, University of Science and Technology (UST), Daejon, 305-343, Republic of Korea
d
Siontech Ltd. R&D Center, 530 Yongsandong, Yuseong-gu, Daejeon, 305-500, Korea
*[email protected]
Recently, the reliable supply of clean fresh water is becoming increasingly difficult as global and regional
development accelerates, and this has become a bottleneck issue for the sustainable development of
many countries. Chestnut-like carbon were prepared PCNFs grown on activated carbons using the catalytic
gasification with Fe - Ni catalysts in air. Catalytic gasification of activated carbon was carried out at 400 for
1 h at each temperature. The PCNFs grown on activated carbon at 600 °C using activated carbon gasified
with a 0.1% Ni-Fe catalyst at 450 °C. The surface area of Chestnut-like carbons were 2401 m2/g. Additional specific capacitances of Chestnut-like carbon are significantly higher than those of other activated
carbons. Chestnut-like carbon electrodes show approximately 44% retention of the specific capacitance,
which is higher than that of the virginity activated carbon. Thus, Chestnut-like carbon electrode can be
predicted to yield better performance in the capacitive deionization (CDI) process.
Multidisciplinary modelling of CDI using optimisation tools: implications for agricultural
applications
Peter Kovalsky and David Waite
School of Civil and Environmental Engineering, University of New South Wales
Posters
[email protected], [email protected]
Capacitive deionization is a viable method of water treatment in an increasing number of small scale and
niche applications but is less cost effective at higher volume applications above the megalitre per day
range. As the per-gram cost of adsorbent materials decreases with advancements in manufacturing and
design, CDI could become the answer to significant environmental challenges of larger scale. The work
presented here addresses the issue of scale up with particular attention given to the accuracy of process
costing and optimisation. Models of the physical aspects of CDI developed by Biesheuvel et al (20091,
20112) are used as the basis of the modelling undertaken here with the optimisation tool AspenTech used
to obtain a more accurate estimate of process level performance as a function of key design and process
variables. In particular, consideration is given to possible CDI configurations within a conceptualised large
scale process and the Aspen modelling package used to examine impact of process variables on cost effectiveness. The implementation of CDI in the simulation environment is undertaken via a custom module
utilising a discretised form of the available physical models of the CDI process. The optimisation package
developed enables rapid identification of suitable applications in situations where reverse osmosis has
shown to be non-viable. In this analysis we focus on treatment of brackish water for use in agriculture/
horticulture with particular attention given to the impacts of water demand and brackish water quality on
optimal choice of process parameters and viability of the proposed technology. Further development of
this modelling framework could provide the impetus to attract the resources needed to further accelerate
the cost reduction process.
References
1. P. M. Biesheuvel, B. van Limpt, A. van der Wal, J. Phys. Chem. C 113 (2009), 5636–5640
2. P.M. Biesheuvel, R. Zhao, S. Porada, A. van der Wal, J. Colloid Interface Sci 360 (2011) 239–248
172
Water Denitrification using Energy-Efficient Capacitive Deionization Technology
D.V. Kudin, V.I. Golota, S.V. Rodionov, I.I. Abubekerov
National Science Center “Kharkov Institute of Physics and Technology”
1, Akademicheskaya St., Kharkov, 61108, Ukraine
[email protected]
Recent water quality monitoring has shown the ingress of nitrates into the groundwater. The over-application of fertilizers results in the increased nitrate level and the exceeding maximum permissible concentration (MPC) for nitrates in many areas around the world that is a big risk for human health. Therefore,
the importance of creation and development of water denitrification technologies grows year after year.
The results of the investigation on nitrate sorption in the CDI units are presented in the paper. The electrodes for the CDI units were manufactured from carbon material SAUT-1C which was modified by titanium. Deposition of titanium coating was made using the Arc-PVD method. Weighted samples of pure
chemicals as well as distilled water were used for preparation of standard aqueous solution. The solution
was circulated in a circle. The total volume of the solution was 4,7 L, and the circulation flow rate of the
solution was 1 L/min. The ion concentration was measured using the potentiometric method, and the
total salt content was controlled using the conductometric method. The measurements were made in a
buffer volume. The programmable low-voltage power supply unit CDS1-5M10 was used to supply the electrochemical module with power. The power supply unit includes five separate modules with each having
the operating voltage range of -1,5 V ÷ +1,5 V as well as the operating current range of 0-10 А.
The typical current and voltage oscillograms of the CDI units within the charging-discharging cycles as well
as the variation in nitrate concentration level of the treated solution are shown in the figure. The decrease
of the nitrate concentration by several times (2-5) to the level below the MPC for nitrates (45 mg/l) was
demonstrated. The adsorption of sodium, potassium, calcium ions and chlorides was also studied. It was
shown that the ion adsorption is inversely proportional to the ion valency in aqueous solution. Thus, for
the same total transferred charge the number of calcium ions being adsorbed on the electrode surface is
twice less than the number of monovalent sodium ions that corresponds to the ion valency. It was also
shown that the specific adsorption ability of the carbon material SAUT-1S modified by titanium for sodium
chloride solution (5000 ppm) is 15,3 mg per 1 g of carbon material.
Therefore, it was shown that the CDI technology can be applied for water denitrification as an energy-efficient method.
Posters
173
Fabrication of composite capacitive deionization electrodes using biochar materials
and conductive membranes
Xia Shang, Junhua Jiang, and Roland D. Cusick.
Graduate Student in Environmental Engineering at University of Illinois-Urbana and Champaign
[email protected]
Capacitive deionization (CDI) is considered as a promising and sustainable technique for energy storage
and brackish water desalination. However, the material selection and fabrication of low cost electrodes
is one of the main limiting factors for large-scale commercial applicaiton of CDI technology. In this study,
composites of low-cost and renewable biochar, produced from woody biomass and a conductive polymer,
PEDOT:PSS (poly(3,4-ethylenedioxythiophene) poly(styrenesulfonate)) are evaluated as CDI electrodes.
PEDOT:PSS is a promising candidate to improve the intra-particle conductivity and ion adsorption capacity
of the electrode system due to its high conductivity, processibility, effective binding material, and environmental stability, and low cost. The compatibility of PEDOT:PSS with mesoporous carbon shows applicable
potential to apply the PEDOT:PSS/tailed-carbon system in CDI chambers. The salt adsorption/desorption
efficiency is measured in constant potential and cyclic voltammetry experiment and the electrochemical
property of the electrode is studied by using impedance spectroscopy. The performance of fabricated
electrodes will be compared to biochar capacitive electrodes fabricated with a conventional binding agent
(i.e. PVDF).
Posters
Keywords: Capacitive deionization, Biochar supercapacitor, Conductive polymers, CDI flow design.
Figure CDI electrode constructed with biochar, stainless steel web, and PEDOT:PSS conductive polymer.
174
Electrokinetic remediation of fine clay soils contaminated by Hydrophobic organic
pollutants
Nataliya Mishchuk, Larisa Lysenko, Elena Rynda, Alexei Shen
Institute of Colloid Chemistry and Water Chemistry of National Academy of Sciences of Ukraine, bulv.Vernadskogo, 42, Kiev-142,
Ukraine, 03680, [email protected]
175
Posters
Active accumulation of hydrophobic organic compounds in the environment sets the task of the development of effective methods directed to their removal from water, sludge and soils. The most problematic
objects for decontamination are dispersions, which contain fine clay components. First of all, due to peculiar surface and volume properties and large specific surface area of this type of dispersions, they are
the most inclined to retain pollution. Secondly, due to the high values of hydrodynamic and aerodynamic
resistances, the choice of effective decontamination method is extremely limited.
Electrokinetic treatment is the method for which the fine clay soil specific properties ensure its effectiveness in removing of uncharged organic compounds. For the effective management of the process it is
necessary to provide a stable electroosmotic flow and to reach water-solubility of hydrophobic contaminants.
The rate of electroosmotic transport depends on the zeta potential of soil particles, which in turn depends
on the pH of a pore solution. Thus, the important aspect of soil decontamination is regulation of pH.
Electrohydrodynamic method of regulation of pH and intensification of electroosmotic permeability for
enhancing the efficiency of the removal of hydrophobic organic compounds is proposed and theoretically
and experimentally substantiated.
Another aspect is the correct choice of surfactants, which provide desorption and movement of hydrophobic contaminants into the pore solution. Cationic surfactants can not be used since clay soils have a negative electrokinetic potential, which decreases upon introduction of positively charged surfactants leading
to a diminution of the electroosmotic velocity. Introduction of anionic surfactants increases the electrokinetic potential of soil particles accelerating electroosmosis, but in the same time these surfactants can
charge the organic compounds leading to their electromigation in the direction opposite to electroosmotic
flow, thereby also slowing down the rate of soil decontamination. Finally, nonionic surfactants do not
charge the organic pollutants and therefore do not affect the velocity of electroosmosis. Thus, they are
the most promising in soil remediation.
Studies of the effect of the type of surfactants on soil remediation efficiency were carried out on a model
system, which is kaolinite contaminated by ortho-chlorotoluene (4.5 mg/g of kaolinite) using non-ionic
surfactants (Triton X-100, Tergitol 5-S-7, Neonol АF-9-12) and anionogenic surfactant (sodium dodecyl
sulfate).
The obtained experimental data demonstrated that the presence of anionic surfactant results in a significant increase of the velocity of electroosmosis in comparison with the velocity at the use of nonionic
surfactants. For example, at the electrokinetic remediation with the use of sodium dodecyl sulfate 160 ml
of electroosmotic liquid (10 volumes of pore solution) passed through the soil during 20 hours, while the
introduction of a Triton X-100 increased the treatment time to 36 hours. However, as expected, anionogenic surfactant significantly reduced decontamination efficiency - 70.7% of residual ortho-chlorotoluene
compared to 26.0% in the case of non-ionic one that is caused by appearance of their own electromigration mobility
The velocities of electroosmosis for different nonionic surfactants are almost the same, but the degree
of pollutant removal is much different. Tergitol 5-S-7 provided decontamination almost at the same level as it was obtained at presence of Triton X-100 (27.7% of the residual ortho-chlorotoluene). The best
results were obtained for Neonol АF-9-12 (at the passage of 160 ml of electroosmotic liquid the residual
ortho-chlorotoluene decreased to 5.7%). The increase of the treatment time allows to decrease the residual ortho-chlorotoluene to the rather small values, however this is accompanied with increase of power
consumption.
Wetsus, centre of excellence for sustainable water technology is a
facilitating intermediary for trend-setting know-how development. Wetsus
creates a unique environment and strategic cooperation for development of
profitable and sustainable state of the art water treatment technology. The
inspiring and multidisciplinary collaboration between 90 companies and
20 EU research institutes in Wetsus results in innovations that contribute
significantly to the solution of the global water problems.

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